Normal alpha olefin synthesis using dehydroformylation or dehydroxymethylation

ABSTRACT

The present invention discloses processes for producing normal alpha olefins, such as 1-hexene, 1-octene, 1-decene, and 1-dodecene in a multistep synthesis scheme from another normal alpha olefin. Also disclosed are reactions for converting aldehydes, primary alcohols, and terminal vicinal diols into normal alpha olefins.

REFERENCE TO RELATED APPLICATION

This application is a continuation application of U.S. patentapplication Ser. No. 16/283,892, filed on Feb. 25, 2019, now U.S. PatentNo. 10,723,672, which claims the benefit of U.S. Provisional PatentApplication No. 62/634,979, filed on Feb. 26, 2018, the disclosures ofwhich are incorporated herein by reference in their entirety.

FIELD OF THE INVENTION

The present disclosure relates generally to methods for making normalalpha olefins from aldehydes, primary alcohols, and terminal vicinaldiols.

BACKGROUND OF THE INVENTION

The synthesis of specific carbon number normal alpha olefins, whetherdirectly from another compound having an alcohol or aldehyde functionalgroup, or via a multistep synthesis scheme from another normal alphaolefin, is of significant importance in the chemical industry. It wouldbe beneficial to develop such reactions and synthesis schemes to producedesirable normal alpha olefin products. Accordingly, it is to these endsthat the present invention is generally directed.

SUMMARY OF THE INVENTION

This summary is provided to introduce a selection of concepts in asimplified form that are further described herein. This summary is notintended to identify required or essential features of the claimedsubject matter. Nor is this summary intended to be used to limit thescope of the claimed subject matter.

Catalyst compositions that can be used in oxidative dehydroxymethylationand oxidative dehydroformylation processes to produce normal alphaolefins are disclosed herein. Such catalyst compositions can comprise atransition metal compound, a phosphine, and a heteroatomic acid orheteroatomic acid derivative, or a phosphine transition metal compoundcomplex and a heteroatomic acid or heteroatomic acid derivative. Thesecatalyst compositions can further comprise an acceptor, which istypically an olefinic compound.

A dehydroxymethylation process consistent with aspects of this inventioncan comprise contacting a saturated linear C₃-C₃₆ hydrocarbon primaryalcohol with the catalyst composition to form a C₂-C₃₅ normal alphaolefin. Another dehydroxymethylation process consistent with aspects ofthis invention can comprise contacting a saturated linear C₄-C₃₆hydrocarbon terminal vicinal diol with the catalyst composition to forma C₂-C₃₄ normal alpha olefin. In yet another aspect, adehydroformylation process is disclosed, and the dehydroformylationprocess can comprise contacting a saturated linear C₃-C₃₆ hydrocarbonaldehyde with the catalyst composition to form a C₂-C₃₅ normal alphaolefin.

Processes for producing normal alpha olefins using multistep synthesisschemes also are disclosed and described herein. One such process cancomprise (i) conducting a hydroboration-oxidation reaction of a firstnormal alpha olefin having the structure CH₃(CH₂)_(n)HC═CH₂ to form alinear primary alcohol having the structure CH₃(CH₂)_(n+1)CH₂OH, and(ii) contacting the linear primary alcohol with a dehydroxymethylationcatalyst composition to form a second normal alpha olefin having thestructure CH₃(CH₂)_(n−1)HC═CH₂. Another process can comprise (i)conducting a dihydroxylation reaction of a first normal alpha olefinhaving the structure CH₃(CH₂)_(n)HC═CH₂ to form a terminal vicinal diolhaving the structure CH₃(CH₂)_(n)CH(OH)CH₂OH, and (ii) contacting theterminal vicinal diol with a dehydroxymethylation catalyst compositionto form a second normal alpha olefin having the structureCH₃(CH₂)_(n−2)HC═CH₂. In these processes, n is an integer that can rangefrom 2 to 33.

Another process for producing a normal alpha olefin using a multistepsynthesis scheme can comprise (i) contacting a first normal alpha olefinhaving the structure CH₃(CH₂)_(n)HC═CH₂ and a metathesis catalyst systemto form a linear internal olefin having the structureCH₃(CH₂)_(n)HC═CH(CH₂)_(n)CH₃, (ii) contacting the linear internalolefin with a hydroformylation catalyst system, carbon monoxide, andhydrogen to form a linear aldehyde having the formulaCH₃(CH₂)_(2n+3)C(═O)H, and (iii) contacting the linear aldehyde with adehydroformylation catalyst composition to form a second normal alphaolefin having the structure CH₃(CH₂)_(2n+1)HC═CH₂. In this process, n isan integer that can range from 0 to 15.

Another process for producing normal alpha olefins consistent withaspects of this invention can comprise (a) contacting a linear internalolefin having the structure CH₃(CH₂)_(p)HC═CH(CH₂)_(q)CH₃ with ahydroformylation catalyst system, carbon monoxide, and hydrogen to forma linear aldehyde having the formula CH₃(CH₂)_(p+q+3)C(═O)H, and (b)contacting the linear aldehyde with a dehydroformylation catalystcomposition to form a normal alpha olefin having the structureCH₃(CH₂)_(p+q+1)HC═CH₂. In this process, p and q can be integers thatindependently range from 0 to 15.

Both the foregoing summary and the following detailed descriptionprovide examples and are explanatory only. Accordingly, the foregoingsummary and the following detailed description should not be consideredto be restrictive. Further, features or variations can be provided inaddition to those set forth herein. For example, certain aspects can bedirected to various feature combinations and sub-combinations describedin the detailed description.

Definitions

To define more clearly the terms used herein, the following definitionsare provided. Unless otherwise indicated, the following definitions areapplicable to this disclosure. If a term is used in this disclosure butis not specifically defined herein, the definition from the IUPACCompendium of Chemical Terminology, 2nd Ed (1997), can be applied, aslong as that definition does not conflict with any other disclosure ordefinition applied herein, or render indefinite or non-enabled any claimto which that definition is applied. To the extent that any definitionor usage provided by any document incorporated herein by referenceconflicts with the definition or usage provided herein, the definitionor usage provided herein controls.

Herein, features of the subject matter can be described such that,within particular aspects, a combination of different features can beenvisioned. For each and every aspect and/or feature disclosed herein,all combinations that do not detrimentally affect the designs,compositions, processes, and/or methods described herein arecontemplated with or without explicit description of the particularcombination. Additionally, unless explicitly recited otherwise, anyaspect and/or feature disclosed herein can be combined to describeinventive features consistent with the present disclosure.

While compositions and processes/methods are described herein in termsof “comprising” various components or steps, the compositions andprocesses/methods can also “consist essentially of” or “consist of” thevarious components or steps, unless stated otherwise. For example, acatalyst composition consistent with aspects of the present inventioncan comprise; alternatively, can consist essentially of; oralternatively, can consist of; a transition metal compound, a phosphine,and a heteroatomic acid or heteroatomic acid derivative.

The terms “a,” “an,” and “the” are intended to include pluralalternatives, e.g., at least one, unless otherwise specified. Forinstance, the disclosure of “a normal alpha olefin” or “an acceptor” ismeant to encompass one, or combinations of more than one, normal alphaolefin or acceptor, respectively, unless otherwise specified.

Generally, groups of elements are indicated using the numbering schemeindicated in the version of the periodic table of elements published inChemical and Engineering News, 63(5), 27, 1985. In some instances, agroup of elements can be indicated using a common name assigned to thegroup; for example, alkali metals for Group 1 elements, alkaline earthmetals for Group 2 elements, transition metals for Group 3-12 elements,and halogens or halides for Group 17 elements.

For any particular compound or group disclosed herein, any name orstructure presented is intended to encompass all conformational isomers,regioisomers, stereoisomers, and mixtures thereof that can arise from aparticular set of substituents, unless otherwise specified. The name orstructure also encompasses all enantiomers, diastereomers, and otheroptical isomers (if there are any), whether in enantiomeric or racemicforms, as well as mixtures of stereoisomers, as would be recognized by askilled artisan, unless otherwise specified. For example, a generalreference to hexene (or hexenes) includes all linear or branched,acyclic or cyclic, hydrocarbon compounds having six carbon atoms and 1carbon-carbon double bond; a general reference to pentane includesn-pentane, 2-methyl-butane, and 2,2-dimethylpropane; a general referenceto a butyl group includes an n-butyl group, a sec-butyl group, aniso-butyl group, and a t-butyl group; and a general reference tocyclododecatriene includes all isomeric forms (e.g.,trans,trans,cis-1,5,9-cyclododecatriene, andtrans,trans,trans-1,5,9-cyclododecatriene, among other dodecatrienes).

The terms “contact product,” “contacting,” and the like, are used hereinto describe compositions and methods wherein the components arecontacted or combined together in any order, in any manner, and for anylength of time, unless otherwise specified. For example, the componentscan be contacted by blending or mixing. Further, unless otherwisespecified, the contacting of any component can occur in the presence orabsence of any other component of the compositions and methods describedherein. Combining additional materials or components can be done by anysuitable method. Further, the term “contact product” includes mixtures,blends, solutions, slurries, reaction products, and the like, orcombinations thereof. Although “contact product” can, and often does,include reaction products, it is not required for the respectivecomponents to react with one another. Similarly, the term “contacting”is used herein to refer to materials which can be blended, mixed,slurried, dissolved, reacted, treated, or otherwise combined in someother manner. Hence, “contacting” two or more components can result in amixture, a reaction product, a reaction mixture, etc.

The terms “catalyst composition,” “catalyst mixture,” “catalyst system,”and the like, do not depend upon the actual product or compositionresulting from the contact or reaction of the initial components of thedisclosed or claimed catalyst composition/mixture/system, the nature ofthe active catalytic site, or the fate of the transition metal compound,the phosphine, the heteroatomic acid or heteroatomic acid derivative,and the acceptor, after combining these components. Therefore, the terms“catalyst composition,” “catalyst mixture,” “catalyst system,” and thelike, encompass the initial starting components of the composition, aswell as whatever product(s) may result from contacting these initialstarting components, and this is inclusive of both heterogeneous andhomogenous catalyst systems or compositions. The terms “catalystcomposition,” “catalyst mixture,” “catalyst system,” and the like, canbe used interchangeably throughout this disclosure.

The term “hydrocarbon” whenever used in this specification and claimsrefers to a compound containing only carbon and hydrogen. The term“olefin” as used herein refers to a hydrocarbon that has at least onecarbon-carbon double bond that is not part of an aromatic ring or ringsystem. The term “olefin” includes aliphatic and aromatic, cyclic andacyclic, and/or linear and branched compounds having at least onecarbon-carbon double bond that is not part of an aromatic ring or ringsystem, unless specifically stated otherwise. Olefins having only one,only two, only three, etc., carbon-carbon double bonds can be identifiedby use of the term “mono,” “di,” “tri,” etc., within the name of theolefin. The olefins can be further identified by the position of thecarbon-carbon double bond(s). The term “alpha olefin” as used hereinrefers to any olefin that has a double bond between the first and secondcarbon atom of a contiguous chain of carbon atoms. The term “alphaolefin” includes linear and branched alpha olefins and alpha olefinswhich can have more than one non-aromatic carbon-carbon double bond,unless expressly stated otherwise.

The term “normal alpha olefin” as used herein refers to a linearaliphatic hydrocarbon mono-olefin having a double bond between the firstand second carbon atom. The term “linear internal olefin” as used hereinrefers to a linear aliphatic hydrocarbon mono-olefin having a doublebond that is not between the first and second carbon atom, can befurther described by the chemical formulas provided throughout thisdisclosure.

An “aromatic compound” refers to a compound containing a cyclicallyconjugated moiety that follows the Hückel (4n+2) rule and containing(4n+2) pi-electrons, where n is an integer from 1 to about 5. Aromaticcompounds can be monocyclic or polycyclic, unless otherwise specified.Non-limiting examples of aromatic compounds include benzene,naphthalene, and toluene, among others.

As utilized herein, the term “solvent” applies to a material which candissolve a compound, or a material which can dilute the components of areaction. As such, the term “solvent” can encompass materials which canact as a diluent, unless stated otherwise.

Several types of ranges are disclosed in the present invention. When arange of any type is disclosed or claimed, the intent is to disclose orclaim individually each possible number that such a range couldreasonably encompass, including end points of the range as well as anysub-ranges and combinations of sub-ranges encompassed therein. Forexample, when a chemical moiety having a certain number of carbon atomsis disclosed or claimed, the intent is to disclose or claim individuallyevery possible number that such a range could encompass, consistent withthe disclosure herein. For example, the disclosure that a moiety is a C₁to C₁₈ hydrocarbyl group, or in alternative language, a hydrocarbylgroup having from 1 to 18 carbon atoms, as used herein, refers to amoiety that can have 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15,16, 17, or 18 carbon atoms, as well as any range between these twonumbers (for example, a C₁ to C₈ hydrocarbyl group), and also includingany combination of ranges between these two numbers (for example, a C₂to C₄ and a C₁₂ to C₁₆ hydrocarbyl group).

The term “about” means that amounts, sizes, formulations, parameters,and other quantities and characteristics are not and need not be exact,but can be approximate including being larger or smaller, as desired,reflecting tolerances, conversion factors, rounding off, measurementerrors, and the like, and other factors known to those of skill in theart. In general, an amount, size, formulation, parameter or otherquantity or characteristic is “about” or “approximate” whether or notexpressly stated to be such. The term “about” also encompasses amountsthat differ due to different equilibrium conditions for a compositionresulting from a particular initial mixture. Whether or not modified bythe term “about,” the claims include equivalents to the quantities. Theterm “about” can mean within 10% of the reported numerical value,preferably within 5% of the reported numerical value.

Although any methods and materials similar or equivalent to thosedescribed herein can be used in the practice or testing of theinvention, the typical methods and materials are herein described.

All publications and patents mentioned herein are incorporated herein byreference for the purpose of describing and disclosing, for example, theconstructs and methodologies that are described in the publications,which might be used in connection with the presently describedinvention.

DETAILED DESCRIPTION OF THE INVENTION

The present invention is directed generally to catalyst compositions,processes for using the catalyst compositions in oxidativedehydroxymethylation and oxidative dehydroformylation reactions toproduce normal alpha olefins, and multistep synthesis schemes to converta normal alpha olefin into a different normal alpha olefin (i.e., with adifferent number of carbon atoms).

Beneficially, the disclosed processes can selectively produce normalalpha olefins, while minimizing byproduct alkanes and internal olefins.Also beneficially, the disclosed processes can convert odd carbon numberalcohols or aldehydes to even carbon number olefins, and even carbonnumber diols to even carbon number olefins.

Catalyst Compositions

While not limited thereto, the catalyst compositions disclosed hereincan be used in oxidative dehydroxymethylation processes to convertalcohol compounds to normal alpha olefins, and oxidativedehydroformylation processes to convert aldehyde compounds to normalalpha olefins. The catalyst composition can utilize a pre-formed orpre-synthesized transition metal complex, or one in which the componentsare added together to generate the complex and catalyst in-situ. Thus,for example, the catalyst composition can comprise any suitabletransition metal compound, any suitable phosphine, and any suitableheteroatomic acid or heteroatomic acid derivative. Generally, thetransition metal compound, the phosphine, and the heteroatomic acid orheteroatomic acid derivative are independent elements of the catalystcomposition and are independently described herein. Consequently, thecatalyst composition can be described utilizing any combination of thetransition metal compound disclosed herein, the phosphine disclosedherein, and the heteroatomic acid or heteroatomic acid derivativedisclosed herein. In another aspect, the catalyst composition cancomprise any suitable phosphine transition metal compound complex andany suitable heteroatomic acid or heteroatomic acid derivative. In thiscatalyst composition aspect, the phosphine transition metal compoundcomplex and the heteroatomic acid or heteroatomic acid derivative areindependent elements of the catalyst composition and are independentlydescribed herein. Consequently, the catalyst composition can bedescribed utilizing any combination of the phosphine transition metalcompound complex disclosed herein and the heteroatomic acid orheteroatomic acid derivative disclosed herein.

The transition metal of the transition metal compound or the phosphinetransition metal compound complex can be a Group 3 to Group 10transition metal, a Group 4 to Group 11 transition metal, a Group 4 toGroup 9 transition metal, a Group 8 to Group 10 transition metal, or aGroup 9 transition metal. For instance, the transition metal of thetransition metal compound or the phosphine transition metal compoundcomplex can be cobalt, rhodium, or iridium; alternatively, cobalt;alternatively, rhodium; or alternatively, iridium. Accordingly, in anaspect of this invention, the transition metal compound or thetransition metal compound of the phosphine transition metal compoundcomplex can comprise a rhodium compound, non-limiting examples of whichcan include an olefin rhodium alkoxide complex, a cyclodiene rhodiumalkoxide complex, or any combination thereof alternatively, an olefinrhodium alkoxide complex; or alternatively, a cyclodiene rhodiumalkoxide complex.

In one aspect, the phosphine or the phosphine of the phosphinetransition metal compound complex can be a monophosphine. Illustrativeand non-limiting examples of monophosphines include an alkyl phosphine(e.g., trimethylphosphine, triethylphosphine, triisopropylphosphine,triadamantylphosphine, and the like), an aryl phosphine (e.g.,triphenylphosphine, tri-p-tolylphosphine, and the like), or anycombination thereof.

In another aspect, the phosphine or the phosphine of the phosphinetransition metal compound complex can be a diphosphine having thefollowing structure:

In structure (I), L¹ can be any suitable linking group or any linkinggroup disclosed herein, and each R independently can be H or any C₁ toC₁₈ hydrocarbyl group, C₁ to C₁₈ hydrocarboxy group, or C₁ to C₁₈hydrocarbylaminyl group disclosed herein. For instance, each Rindependently can be H or a C₁ to C₁₂ hydrocarbyl group; alternatively,H or a C₁ to C₆ hydrocarbyl group; alternatively, H or a C₁ to C₁₈ alkylgroup, C₂ to C₁₈ alkenyl group, C₆ to C₁₈ aryl group, or C₇ to C₁₈aralkyl group; or alternatively, H or a C₁ to C₅ alkyl group, C₂ to C₅alkenyl group, C₆ to C₈ aryl group, or C₇ to C₈ aralkyl group. Each Rindependently in structure (I) can be, in certain aspects, H, a methylgroup, an ethyl group, a propyl group, a butyl group, a pentyl group, ahexyl group, a heptyl group, an octyl group, a nonyl group, a decylgroup, an ethenyl group, a propenyl group, a butenyl group, a pentenylgroup, a hexenyl group, a heptenyl group, an octenyl group, a nonenylgroup, a decenyl group, a phenyl group, a tolyl group, a benzyl group,or a naphthyl group. In other aspects, each R independently can be H, amethyl group, an ethyl group, a propyl group, a butyl group, a pentylgroup, a hexyl group, a heptyl group, an octyl group, a nonyl group, ora decyl group; alternatively, H, an ethenyl group, a propenyl group, abutenyl group, a pentenyl group, a hexenyl group, a heptenyl group, anoctenyl group, a nonenyl group, or a decenyl group; or alternatively, H,a phenyl group, a tolyl group, a benzyl group, or a naphthyl group.

A hydrocarboxy group is used generically herein to include, forinstance, alkoxy, aryloxy, aralkoxy, -(alkylene, arylene, oraralkylene)-O-(alkyl, aryl, or aralkyl) groups, and —O(CO)-(hydrogen orhydrocarbyl) groups, and these groups can comprise up to about 18 carbonatoms (e.g., C₁ to C₁₈, C₁ to C₁₀, or C₁ to C₈ hydrocarboxy groups).Cyclic groups also are included. Illustrative and non-limiting examplesof hydrocarboxy groups can include, but are not limited to, a methoxygroup, an ethoxy group, an n-propoxy group, an isopropoxy group, ann-butoxy group, a sec-butoxy group, an isobutoxy group, a tert-butoxygroup, an n-pentoxy group, a 2-pentoxy group, a 3-pentoxy group, a2-methyl-1-butoxy group, a tert-pentoxy group, a 3-methyl-1-butoxygroup, a 3-methyl-2-butoxy group, a neo-pentoxy group, a phenoxy group,a toloxy group, a xyloxy group, a 2,4,6-trimethylphenoxy group, abenzoxy group, an acetylacetonate group (acac), a formate group, anacetate group, a stearate group, an oleate group, a benzoate group, atetrahydrofuran group, a 1,4-dioxane group, and the like. In an aspect,the hydrocarboxy group which can be a R in formula (I) can be a methoxygroup; alternatively, an ethoxy group; alternatively, an n-propoxygroup; alternatively, an isopropoxy group; alternatively, an n-butoxygroup; alternatively, a sec-butoxy group; alternatively, an isobutoxygroup; alternatively, a tert-butoxy group; alternatively, an n-pentoxygroup; alternatively, a 2-pentoxy group; alternatively, a 3-pentoxygroup; alternatively, a 2-methyl-1-butoxy group; alternatively, atert-pentoxy group; alternatively, a 3-methyl-1-butoxy group,alternatively, a 3-methyl-2-butoxy group; alternatively, a neo-pentoxygroup; alternatively, a phenoxy group; alternatively, a toloxy group;alternatively, a xyloxy group; alternatively, a 2,4,6-trimethylphenoxygroup; alternatively, a benzoxy group; alternatively, an acetylacetonategroup; alternatively, a formate group; alternatively, an acetate group;alternatively, a stearate group; alternatively, an oleate group;alternatively, a benzoate group; alternatively, a tetrahydrofuran group;or alternatively, a 1,4-dioxane group.

The term hydrocarbylaminyl group is used generically herein to refercollectively to, for instance, alkylaminyl, arylaminyl, aralkylaminyl,dialkylaminyl, diarylaminyl, diaralkylaminyl, -(alkylene, arylene, oraralkylene)-N-(alkyl, aryl, or aralkyl) groups, and cyclic and aromaticamine groups (e.g., piperidine groups, pyrrole groups), and unlessotherwise specified, the hydrocarbylaminyl groups can comprise up toabout 18 carbon atoms (e.g., C₁ to C₁₈, C₁ to C₁₀, or C₁ to C₈hydrocarbylaminyl groups). Accordingly, hydrocarbylaminyl is intended tocover both (mono)hydrocarbylaminyl and dihydrocarbylaminyl groups. Insome aspects, the hydrocarbylaminyl group can be, for instance, amethylaminyl group (—NHCH₃), an ethylaminyl group (—NHCH₂CH₃), ann-propylaminyl group (—NHCH₂CH₂CH₃), an iso-propylaminyl group(—NHCH(CH₃)₂), an n-butylaminyl group (—NHCH₂CH₂CH₂CH₃), a t-butylaminylgroup (—NHC(CH₃)₃), an n-pentylaminyl group (—NHCH₂CH₂CH₂CH₂CH₃), aneo-pentylaminyl group (—NHCH₂C(CH₃)₃), a phenylaminyl group (—NHC₆H₅),a tolylaminyl group (—NHC₆H₄CH₃), or a xylylaminyl group(—NHC₆H₃(CH₃)₂); alternatively, a methylaminyl group; alternatively, anethylaminyl group; alternatively, a propylaminyl group; oralternatively, a phenylaminyl group. In other aspects, thehydrocarbylaminyl group which can be, for instance, a dimethylaminylgroup (—N(CH₃)₂), a diethylaminyl group (—N(CH₂CH₃)₂), adi-n-propylaminyl group (—N(CH₂CH₂CH₃)₂), a di-iso-propylaminyl group(—N(CH(CH₃)₂)₂), a di-n-butylaminyl group (—N(CH₂CH₂CH₂CH₃)₂), adi-t-butylaminyl group (—N(C(CH₃)₃)₂), a di-n-pentylaminyl group(—N(CH₂CH₂CH₂CH₂CH₃)₂), a di-neo-pentylaminyl group (—N(CH₂C(CH₃)₃)₂), adi-phenylaminyl group (—N(C₆H₅)₂), a di-tolylaminyl group(—N(C₆H₄CH₃)₂), or a di-xylylaminyl group (—N(C₆H₃(CH₃)₂)₂);alternatively, a dimethylaminyl group; alternatively, a di-ethylaminylgroup; alternatively, a di-n-propylaminyl group; or alternatively, adi-phenylaminyl group.

In one aspect, the phosphine or the phosphine of the phosphinetransition metal compound complex can comprise (or consist essentiallyof, or consist of) a 1,6-bis(dihydro-carbylphosphinyl)hexane, asubstituted 1,6-bis(dihydrocarbylphosphinyl)hexane, a(1,3-phenylenedi-1,1-ethanediyl)bis(dihydrocarbylphosphine), asubstituted (1,3-phenylenedi-1,1-ethanediyl)bis(dihydrocarbylphosphine),a 1,8-anthracenediylbis(dihydrocarbylphosphine), a substituted1,8-anthracenediylbis(dihydrocarbylphosphine), a1,8-tetradecahydroanthracenediylbis(dihydrocarbylphosphine), asubstituted 1,8-tetradecahydroanthracenediylbis(dihydrocarbylphosphine),a (methylenedi-2,1-phenylene)bis(dihydrocarbylphosphine), a substituted(methylenedi-2,1-phenylene)bis(dihy drocarbylphosphine), a9H-xanthene-4,5-diylbis(dihydrocarbylphosphine), or a substituted9H-xanthene-4,5-diylbis(dihydrocarbylphosphine). For example, thephosphine or the phosphine of the phosphine transition metal compoundcomplex can comprise (or consist essentially of, or consist of) a1,6-bis(dihydrocarbylphosphinyl)hexane; alternatively, a substituted1,6-bis(dihydrocarbylphosphinyl)hexane; alternatively, a(1,3-phenylenedi-1,1-ethanediyl)-bis(dihydrocarbylphosphine);alternatively, a substituted(1,3-phenylenedi-1,1-ethanediyl(bis-(dihydrocarbylphosphine);alternatively, a 1,8-anthracenediylbis(dihydrocarbylphosphine);alternatively, a substituted1,8-anthracenediylbis(dihydrocarbylphosphine); alternatively, a1,8-tetradecahydroanthracenediylbis(dihydrocarbylphosphine);alternatively, a substituted1,8-tetradecahydroanthracenediylbis(dihydrocarbylphosphine);alternatively, a (methylenedi-2,1-phenylene)bis(dihydrocarbylphosphine);alternatively, a substituted(methylenedi-2,1-phenylene)bis(dihydrocarbylphosphine); alternatively, a9H-xanthene-4,5-diylbis(dihydrocarbylphosphine); or alternatively, asubstituted 9H-xanthene-4,5-diylbis(dihydrocarbylphosphine). Eachhydrocarbyl independently can be any suitable hydrocarbyl group or anyC₁ to C₁₈ hydrocarbyl group, C₁ to C₁₂ hydrocarbyl group, or C₁ to C₆hydrocarbyl group disclosed herein.

In another aspect, the phosphine or the phosphine of the phosphinetransition metal compound complex can comprise (or consist essentiallyof, or consist of) a 1,6-bisphosphinylhexane, a substituted1,6-bisphosphinylhexane, a(1,3-phenylenedi-1,1-ethanediyl)bis(phosphine), a substituted(1,3-phenylenedi-1,1-ethanediyl)bis(phosphine), a1,8-anthracenediylbis(phosphine), a substituted1,8-anthracenediylbis(phosphine), a1,8-tetradecahydroanthracenediylbis(phosphine), a substituted1,8-tetradecahydroanthracenediylbis(phosphine), a(methylenedi-2,1-phenylene)bis(phosphine), a substituted(methylenedi-2,1-phenylene)bis(phosphine), a9H-xanthene-4,5-diylbis(phosphine), or a substituted9H-xanthene-4,5-diylbis(phosphine). For example, the phosphine or thephosphine of the phosphine transition metal compound complex cancomprise (or consist essentially of, or consist of) a1,6-bisphosphinylhexane; alternatively, a substituted1,6-bisphosphinylhexane; alternatively, a(1,3-phenylenedi-1,1-ethanediyl)bis(phosphine); alternatively, asubstituted (1,3-phenylenedi-1,1-ethanediyl)bis(phosphine);alternatively, a 1,8-anthracenediylbis(phosphine); alternatively, asubstituted 1,8-anthracenediylbis(phosphine); alternatively, a1,8-tetradecahydroanthracene-diylbis(phosphine); alternatively, asubstituted 1,8-tetradecahydroanthracenediylbis(phosphine);alternatively, a (methylenedi-2,1-phenylene)bis(phosphine);alternatively, a substituted (methylenedi-2,1-phenylene)bis(phosphine);alternatively, a 9H- xanthene-4,5-diylbis(phosphine); or alternatively,a substituted 9H-xanthene-4,5-diylbis(phosphine).

In yet another aspect, the phosphine or the phosphine of the phosphinetransition metal compound complex can comprise (or consist essentiallyof, or consist of) a (9,9-dimethyl-9H-xanthen-4,5-diyl)bis(phosphine) ora substituted (9,9-dimethyl-9H-xanthen-4,5-diyl)bis(phosphine);alternatively, a (9,9-dimethyl-9H-xanthen-4,5-diylbis(phosphine); oralternatively, a substituted(9,9-dimethyl-9H-xanthen-4,5-diyl)bis(phosphine).

In still another aspect, the phosphine or the phosphine of thetransition metal compound complex can have any one of the followingstructures, wherein Ph is a phenyl group, and each R independently canbe H or any C₁ to C₁₈ hydrocarbyl group, C₁ to C₁₈ hydrocarboxy group,or C₁ to C₁₈ hydrocarbylaminyl group disclosed herein (e.g., H, a C₁ toC₁₂ hydrocarbyl group, a C₁ to C₁₂ hydrocarboxy group, or C₁ to C₁₂hydrocarbylaminyl group; alternatively, H or a C₁ to C₆ hydrocarbylgroup; alternatively, H or a C₁ to C₁₈ alkyl group, C₂ to C₁₈ alkenylgroup, C₆ to C₁₈ aryl group, or C₇ to C₁₈ aralkyl group; oralternatively, H or a C₁ to C₅ alkyl group, C₂ to C₅ alkenyl group, C₆to C₈ aryl group, or C₇ to C₈ aralkyl group):

In another aspect, the phosphine or the phosphine of the transitionmetal compound complex can have any one of the following structures,wherein Ph is a phenyl group, Me is a methyl group, Ar is an aromaticgroup, each R independently can be H or any C₁ to C₁₈ hydrocarbyl group,C₁ to C₁₈ hydrocarboxy group, or C₁ to C₁₈ hydrocarbylaminyl groupdisclosed herein, and L can be any linking group disclosed herein.

Any suitable linking group (L or L¹ in the above structures/formulas)can be used. For instance, the linking group can be any hydrocarbylenegroup (e.g., alkylene, cycloalkylene, or arylene), hydrocarboxy group(e.g., ether or cyclic ether), or hydrocarbylaminyl group disclosedherein.

The specific heteroatomic acid or heteroatomic acid derivative used inthe catalyst composition is not particularly limited. In some aspects,the heteroatomic acid or heteroatomic acid derivative can comprise acarboxylic acid, an alcohol, a mineral acid, an ammonium salt, an amine,a thiol, and the like, as well as combinations thereof. For instance,the heteroatomic acid or heteroatomic acid derivative can comprise acarboxylic acid or carboxylic acid derivative. In one aspect, thecarboxylic acid or carboxylic acid derivative can be an aliphaticcarboxylic acid or carboxylic acid derivative, while in another aspect,the carboxylic acid or carboxylic acid derivative can be an aromaticcarboxylic acid or carboxylic acid derivative. The carboxylic acid canbe any suitable C₁ to C₂₄ carboxylic acid or any C₁ to C₂₄ carboxylicacid disclosed herein, either substituted or unsubstituted. Non-limitingexamples of carboxylic acids can include formic acid, acetic acid,propionic acid, butanoic acid, pentanoic acid, hexanoic acid, stearicacid, acrylic acid, methacrylic acid, cinnamic acid, benzoic acid,salicylic acid, adipic acid, citric acid, or any combination thereof.

As used herein, “heteroatomic acid derivative” and “carboxylic acidderivative” are meant to encompass salts and esters of heteroatomicacids and carboxylic acids, respectively. For instance, the carboxylicacid derivative can be a carboxylic acid salt, a carboxylic acid ester,or any combination thereof; alternatively, a carboxylic acid salt; oralternatively, a carboxylic acid ester. Typical carboxylic acid saltscan include alkali metal or alkaline earth metal salts (e.g., sodium,calcium, magnesium) of the carboxylic acid, while esters refers tocompounds where at least one —OH group of the carboxylic acid isreplaced by an alkoxy group (e.g., formates, acetates, hexanoates,stearates, acrylates, cinnamates, benzoates, and the like). Similar tothe carboxylic acid, the carboxylic acid derivative can be any suitableC₁ to C₂₄ carboxylic acid derivative or any C₁ to C₂₄ carboxylic acidderivative disclosed herein, either substituted or unsubstituted. In anaspect, each substituent can be a C₁ to C₈ hydrocarbyl group, a C₁ to C₅hydrocarbyl group, a C₁ to C₈ alkyl group, or a C₁ to C₅ alkyl group. Inan aspect, the carboxylic acid ester can be a methyl ester, an ethylester, a propyl ester, or a butyl ester of any carboxylic acid describedherein. As a representative example, the carboxylic acid or carboxylicacid derivative can comprise benzoic acid (or a substituted benzoicacid) or a salt or ester of benzoic acid (or a salt or ester of asubstituted benzoic acid).

In circumstances where the catalyst composition comprises a transitionmetal compound, a phosphine, and a heteroatomic acid or heteroatomicacid derivative, the minimum molar ratio of the transition metal (of thetransition metal compound) to the phosphine can be 0.2:1, 0.5:1, 0.8:1,or 0.95:1; additionally or alternatively, the maximum molar ratio of thetransition metal to the phosphine can be 5:1, 4:1, 3:1, or 2.5:1. In anaspect, the transition metal (of the transition metal compound) tophosphine (or diphosphine) molar ratio can be in a range from anyminimum transition metal to phosphine molar ratio disclosed herein toany maximum transition metal to phosphine molar ratio disclosed herein.In some non-limiting aspects, the molar ratio can be in a range fromabout 0.2:1 to about 5:1, from about 0.2:1 to about 3:1, from about0.5:1 to about 4:1, or from about 0.95:1 to about 2.5:1. Other molarratios of the transition metal to the phosphine (or diphosphine) arereadily apparent from this disclosure.

The amount of the heteroatomic acid or heteroatomic acid derivative usedin the catalyst composition is not particularly limited, but generally,the minimum molar ratio of the transition metal (of the transition metalcompound or the phosphine transition metal compound complex) to theheteroatomic acid or heteroatomic acid derivative can be 0.8:1, 0.85:1,0.9:1, or 0.95:1; additionally or alternatively, the maximum molar ratioof the transition metal to the heteroatomic acid or heteroatomic acidderivative can be 5:1, 3:1, 2:1, or 1.5:1. In an aspect, the transitionmetal (of the transition metal compound or the phosphine transitionmetal compound complex) to heteroatomic acid or heteroatomic acidderivative molar ratio can be in a range from any minimum transitionmetal to heteroatomic acid or heteroatomic acid derivative molar ratiodisclosed herein to any maximum transition metal to heteroatomic acid orheteroatomic acid derivative molar ratio disclosed herein. In somenon-limiting aspects, the molar ratio can be in a range from about 0.8:1to about 5:1, from about 0.85:1 to about 3:1, from about 0.9:1 to about2:1, or from about 0.95:1 to about 1.5:1. Other molar ratios of thetransition metal (of the transition metal compound or the phosphinetransition metal compound complex) to the heteroatomic acid orheteroatomic acid derivative are readily apparent from this disclosure.

Beneficially, the catalyst composition can further comprise an acceptor,also referred to as an acceptor olefin, which can increase the yield ofthe normal alpha olefin in the processes described in greater detailhereinbelow. In general, the acceptor can be any suitable compoundhaving at least one carbon-carbon double bond. In an aspect, theacceptor can have at least 2 carbon atoms, at least 3 carbon atoms, atleast 4 carbon atoms, or at least 5 carbon atoms. In some aspects, theacceptor can have a maximum of 100 carbon atoms, 80 carbon atoms, 60carbon atoms, 50 carbon atoms, 40 carbon atoms, 30 carbon atoms, 25carbon atoms, 20 carbon atoms, 15 carbon atoms, or 10 carbon atoms.Generally, the acceptor can have from any minimum number of carbon atomsdescribed herein to any maximum number of carbon atoms described herein.For example, in some non-limiting aspects, the acceptor (or acceptorolefin) can have from 2 to 100 carbon atoms, from 3 to 80 carbon atoms,from 4 to 60 carbon atoms, or from 5 to 60 carbon atoms. Other carbonatom number ranges can be readily envisioned from the present disclosureand are encompassed herein. Mixtures or combinations of more than oneacceptor (or acceptor olefin) can be employed in the present invention.

In an aspect, the acceptor (or acceptor olefin) can be a hydrocarboncompound or, alternatively, a heteroatomic compound. In some aspects,the acceptor can be aliphatic or, alternatively, aromatic. In otheraspects, the acceptor can be acyclic or, alternatively, cyclic.

The acceptor can have at least one carbon-carbon double bond. In oneaspect, the acceptor has from 1 to 10 double bonds; alternatively, from1 to 8 double bonds; alternatively, from 3 to 5 double bonds; oralternatively, from 2 to 4 double bonds. In another aspect, the acceptorcan have only one carbon-carbon double bond; alternatively, only twodouble bonds; alternatively, only three double bonds; alternatively,only four double bonds; alternatively, only five double bonds; oralternatively, only six double bonds.

Representative and non-limiting examples of acceptors (or acceptorolefins) having only one carbon-carbon double bond can comprise, consistessentially of, or consist of, either singly or in any combination,ethylene, t-butyl ethylene, propylene, 1-butene, 2-butene,3-methyl-1-butene, isobutylene, 1-pentene, 2-pentene,3-methyl-1-pentene, 4-methyl-1-pentene, 1-hexene, 2-hexene,3-ethyl-1-hexene, 1-heptene, 2-heptene, 3-heptene, 1-octene, 1-decene,1-undecene, 1-dodecene, 1-tridecene, 1-tetradecene, 1-pentadecene, avinylidene, or styrene.

Representative and non-limiting examples of cyclic acceptor olefinsacceptor having only one carbon-carbon double bond can comprise, consistessentially of, or consist of, either singly or in any combination,norbornene, cyclopentene, cyclohexene, cycloheptene, or cyclooctene. Insome aspects, cyclic acceptor olefins having only one carbon-carbondouble bond can comprise, consist essentially of, or consist of,norbornene; alternatively, cyclopentene; alternatively, cyclohexene;alternatively, cycloheptene; or alternatively, cyclooctene.

Illustrative examples of acceptor olefins having at least twocarbon-carbon double bonds that can be employed in the compositions andprocesses disclosed herein can comprise, consist essentially of, orconsist of, either singly or in any combination, butadiene(1,3-butadiene), isoprene, 1,5-hexadiene, 1,7-octadiene, cyclobutadiene,cyclopentadiene, cyclohexadiene, cyclooctadiene, norbornadiene,vinylcyclohexene, vinylnorbornene, divinylbenzene, or cyclopentadienedimer. Hence, mixtures or combinations of more than one acceptor olefincan be employed. Accordingly, the acceptor olefin having at least twodouble bonds can comprise, consist essentially of, or consist of, eithersingly or in any combination, butadiene, isoprene, 1,5-hexadiene,1,7-octadiene, cyclobutadiene, cyclopentadiene, cyclohexadiene, orcyclooctadiene; alternatively, norbornadiene, vinylcyclohexene,vinylnorbornene, or divinylbenzene; alternatively, butadiene;alternatively, isoprene; alternatively, 1,5-hexadiene; alternatively,1,7-octadiene; alternatively, cyclobutadiene; alternatively,cyclopentadiene; alternatively, cyclohexadiene; alternatively,cyclooctadiene; alternatively, norbornadiene; alternatively,vinylcyclohexene; alternatively, vinylnorbornene; alternatively,divinylbenzene; or alternatively, cyclopentadiene dimer.

In an aspect, the acceptor olefin can comprise, consist essentially of,or consist of, one or more compounds having only three carbon-carbondouble bonds. Illustrative non-limiting examples of such compounds cancomprise, consist essentially of, or consist of, singly or in anycombination, trivinylcyclohexane, trivinylbenzene, cycloheptatriene,dimethyl heptatriene, octatriene, cyclooctatriene, or cyclododecatriene.In one aspect, the acceptor olefin can comprise, consist essentially of,or consist of, trivinylcyclohexane. In another aspect, the acceptorolefin can comprise, consist essentially of, or consist of,trivinylbenzene. In another aspect, the acceptor olefin can comprise,consist essentially of, or consist of, cycloheptatriene. In anotheraspect, the acceptor olefin can comprise, consist essentially of, orconsist of, dimethyl heptatriene. In another aspect, the acceptor olefincan comprise, consist essentially of, or consist of, octatriene. Yet, inanother aspect, the acceptor olefin can comprise, consist essentiallyof, or consist of, cyclooctatriene. In still another aspect, theacceptor olefin can comprise, consist essentially of, or consist of,cyclododecatriene. Additionally, the acceptor can comprise benzene andother aromatic compounds, as well as suitable 1,n-1,x-alkyltrienes(linear alkyltrienes).

Acceptor olefins having four or more carbon-carbon bonds also arecontemplated. For instance, the acceptor olefin can comprise, consistessentially of, or consist of, cyclooctatetraene; alternatively,cyclododecatetraene; alternatively, a polybutadiene; or alternatively, acombination of two or more of these compounds.

In some aspects, the acceptor can comprise, consist essentially of, orconsist of, an unsaturated triglyceride, while in other aspects, theacceptor can comprise, consist essentially of, or consist of, anunsaturated natural source oil. In an aspect, the acceptor can comprise,consist essentially of, or consist of, either singly or in anycombination, soybean oil, corn oil, castor bean oil, or canola oil. Inother aspects, the acceptor can comprise an unsaturated carboxylic acid,an ester of an unsaturated carboxylic acid (e.g., methyl, ethyl ester,propyl, or butyl ester), or any combination thereof alternatively, anunsaturated carboxylic acid; or alternatively, an ester of anunsaturated carboxylic acid. In some aspects, the unsaturated carboxylicacid, or the unsaturated carboxylic acid portion of the unsaturatedcarboxylic acid ester, which can be utilized as the aldehyde groupacceptor can comprise, consist essentially of, or consist of, vinylacetic acid, 3-pentenoic acid, maleic acid, fumaric acid, sorbic acid,caproleic acid, lauroleic acid, myristoleic acid, palmitoleic acid,oleic acid, ricinoleic acid, linoleic acid, linolenic acid, or anycombination thereof. In yet another aspect, the acceptor can comprise anunsaturated carboxylic acid anhydride (e.g., maleic anhydride).

The acceptor also can comprise any suitable heteroatomic olefincompound, either singly or in combination. Representative andnon-limiting examples of such heteroatomic olefin compounds include anenone, an enamine, an enol, an enamide (e.g., acrylamide), and the like,as well as combinations thereof.

Dehydroxymethylation and Dehydroformylation Processes

Aspects of this invention are directed to processes for producing normalalpha olefins from alcohols and aldehydes. A first process (adehydroxymethylation process) consistent with this invention cancomprise contacting a saturated linear C₃-C₃₆ hydrocarbon primaryalcohol with any catalyst composition disclosed herein (e.g., transitionmetal compound, phosphine, heteroatomic acid or derivative, andacceptor) to form a C₂-C₃₅ normal alpha olefin (one carbon is removed inthe conversion of the primary alcohol to the normal alpha olefin). Asecond process (a dehydroxymethylation process) consistent with thisinvention can comprise contacting a saturated linear C₄-C₃₆ hydrocarbonterminal vicinal diol with any catalyst composition disclosed herein toform a C₂-C₃₄ normal alpha olefin (two carbons are removed in theconversion of the diol to the normal alpha olefin). A third process (adehydroformylation process) consistent with this invention can comprisecontacting a saturated linear C₃-C₃₆ hydrocarbon aldehyde with anycatalyst composition disclosed herein to form a C₂-C₃₅ normal alphaolefin (one carbon is removed in the conversion of the aldehyde to thenormal alpha olefin). One or more than one alcohol, diol, or aldehydecan be used in these three processes. Generally, the features of thefirst process, the second process, and the third process (e.g., thenormal alpha olefin, the catalyst system, the alcohol, the diol, thealdehyde, and the conditions under which the reaction is conducted,among other features) are independently described herein and thesefeatures can be combined in any combination to further describe thesethree processes. Moreover, additional process steps can be performedbefore, during, and/or after the steps of these processes, unless statedotherwise.

In the first process, the saturated linear hydrocarbon primary alcoholcan be a C₃-C₃₆ alcohol; alternatively, a C₃-C₂₀ alcohol; oralternatively, a C₅-C₁₇ alcohol. In the second process, the saturatedlinear hydrocarbon terminal vicinal diol can be a C₄-C₃₆ diol;alternatively, a C₄-C₂₀ diol; or alternatively, a C₆-C₁₈ diol. In thethird process, the saturated linear hydrocarbon aldehyde can be a C₃-C₃₆aldehyde; alternatively, a C₃-C₂₀ aldehyde; or alternatively, a C₅-C₁₇aldehyde. Thus, in certain aspects of this invention, the normal alphaolefin that can be produced can comprise a C₂-C₃₅ normal alpha olefin;alternatively, a C₂-C₃₄ normal alpha olefin; alternatively, a C₂-C₁₉normal alpha olefin; alternatively, a C₂-C₁₈ normal alpha olefin; oralternatively, a C₄-C₁₆ normal alpha olefin.

In an aspect of this invention, the normal alpha olefin can comprise,consist essentially of, or consist of, ethylene, propylene, 1-butene,1-pentene, 1-hexene, 1-heptene, 1-octene, 1-nonene, 1-decene,1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene, or anycombination thereof; alternatively, 1-butene, 1-pentene, 1-hexene,1-heptene, 1-octene, or any combination thereof or alternatively,1-butene, 1-pentene, 1-hexene, or any combination thereof. In anotheraspect, the normal alpha olefin can comprise, consist essentially of, orconsist of, 1-butene, 1-hexene, 1-octene, 1-decene, 1-dodecene, or anycombination thereof. In yet another aspect, the normal alpha olefin cancomprise, consist essentially of, or consist of, propylene;alternatively, 1-butene; alternatively, 1-pentene; alternatively,1-hexene; alternatively, 1-heptene; alternatively, 1-octene;alternatively, 1-nonene; alternatively, 1-decene; alternatively,1-dodecene; alternatively, 1-tetradecene; alternatively, 1-hexadecene;or alternatively, 1-octadecene.

The amount of the transition metal in the catalyst composition relativeto the amount of the primary alcohol (or vicinal diol, or linearaldehyde) is not particularly limited. For instance, the minimum molarratio of the primary alcohol (or vicinal diol, or linear aldehyde) tothe transition metal (of the transition metal compound or the phosphinetransition metal compound complex) can be 1:1, 2:1, 5:1, or 10:1;additionally or alternatively, the maximum molar ratio of the primaryalcohol (or vicinal diol, or linear aldehyde) to the transition metalcan be 10,000:1, 1000:1, 500:1, or 250:1. In an aspect, the primaryalcohol (or vicinal diol, or linear aldehyde) to transition metal (ofthe transition metal compound or the phosphine transition metal compoundcomplex) molar ratio can be in a range from any minimum molar ratiodisclosed herein to any maximum molar ratio disclosed herein. In somenon-limiting aspects, the molar ratio can be in a range from 1:1 to10,000:1, from 2:1 to 1000:1, from 5:1 to 500:1, or from 10:1 to 250:1.Other molar ratios of the primary alcohol (or vicinal diol, or linearaldehyde) to transition metal are readily apparent from this disclosure.As those skilled in the art would readily recognize, the primary alcohol(or vicinal diol, or linear aldehyde) to transition metal molar ratiocan change as the dehydroxymethylation or dehydroformylation reactionproceeds. Accordingly, these ranges of molar ratios are meant toencompass the initial ratio as well as any molar ratio of the primaryalcohol (or vicinal diol, or linear aldehyde) to transition metalencountered as the dehydroxymethylation or dehydroformylation reactionproceeds.

In an aspect of this invention, the first process, the second process,and the third process can be conducted in the substantial absence of anacceptor (or an acceptor olefin)—i.e., the process can be conducted“acceptorless.” Generally, in the substantial absence of an acceptormeans that the formation of the normal alpha olefin is performed withless than 1, 0.5, 0.25, 0.1, 0.05, 0.025, or 0.01 mole % of an acceptor,based upon the amount of the primary alcohol (or vicinal diol, or linearaldehyde).

When used, the amount of the acceptor is not particularly limited. Forinstance, the normal alpha olefin can be formed at a minimum acceptor(or acceptor olefin) to primary alcohol (or vicinal diol, or linearaldehyde) molar ratio of 0.2:1, 0.5:1, 0.75:1, 1:1, 1.5:1, or 2:1; oradditionally or alternatively, at a maximum acceptor to primary alcohol(or vicinal diol, or linear aldehyde) molar ratio of 1000:1, 500:1,100:1, 50:1, 25:1, 10:1, or 5:1. In an aspect, the acceptor to primaryalcohol (or vicinal diol, or linear aldehyde) molar ratio can be in arange from any minimum molar ratio disclosed herein to any maximum molarratio disclosed herein. In some non-limiting aspects, the molar ratiocan be in a range from 0.2:1 to 1000:1, from 0.5:1 to 500:1, from 0.75:1to 100:1, from 1:1 to 10:1, or from 0.5:1 to 5:1. Other molar ratios ofthe acceptor to the primary alcohol (or vicinal diol, or linearaldehyde) are readily apparent from this disclosure. As those skilled inthe art would readily recognize, the acceptor to primary alcohol (orvicinal diol, or linear aldehyde) molar ratio can change as thedehydroxymethylation or dehydroformylation reaction proceeds.Accordingly, these ranges of molar ratios are meant to encompass theinitial reactant ratio as well as any molar ratio of the acceptor to theprimary alcohol (or vicinal diol, or linear aldehyde) encountered as thedehydroxymethylation or dehydroformylation reaction proceeds.

The first process, second process, and third process for forming thenormal alpha olefin can be conducted at a variety of temperatures,pressures, and time periods. For instance, the temperature at which theprimary alcohol (or vicinal diol, or linear aldehyde) and the catalystsystem (with or without acceptor) are initially combined can be the sameas, or different from, the temperature at which the normal alpha olefinis formed. As an illustrative example, the primary alcohol (or vicinaldiol, or linear aldehyde) and the catalyst system (with or withoutacceptor) can be initially charged or combined at temperature T1 and,after this initial charging of these materials, the temperature can bechanged to a temperature T2 to allow for the reaction to proceed to formthe normal alpha olefin. Likewise, the pressure can be varied throughoutthe process.

In an aspect, the first process, second process, and third process canbe conducted and/or the normal alpha olefin can be formed at anysuitable temperature. For instance, the first process, second process,and third process can be conducted and/or the normal alpha olefin can beformed at a minimum temperature of 0° C., 10° C., 15° C., or 20° C.;additionally or alternatively, at a maximum temperature of 150° C., 125°C., 100° C., or 75° C. In an aspect, the first process, second process,and third process can be conducted and/or the normal alpha olefin can beformed in a range from any minimum temperature disclosed herein to anymaximum temperature disclosed herein. In some non-limiting aspects, thetemperature can be in a range from 0° C. to 150° C.; alternatively, from0° C. to 100° C.; alternatively, from 10° C. to 125° C.; alternatively,from 10° C. to 75° C.; alternatively, from 15° C. to 150° C.;alternatively, from 15° C. to 100° C.; alternatively, from 20° C. to125° C.; or alternatively, from 20° C. to 75° C. Other temperatureranges are readily apparent from this disclosure. These temperatureranges also are meant to encompass circumstances where the firstprocess, second process, and third process are conducted and/or thenormal alpha olefin is formed at a series of different temperatures,instead of at a single fixed temperature, falling within the respectivetemperature ranges.

Generally, the first process, second process, and third process can beconducted and/or the normal alpha olefin can be formed at any suitablepressure, and this can vary depending upon the particular acceptor thatis used (e.g., to maintain the acceptor in the liquid phase). Forinstance, the first process, second process, and third process can beconducted and/or the normal alpha olefin can be formed at a minimumpressure of 0 psig (0 kPa), 5 psig (34 kPa), or 10 psig (69 kPa);additionally or alternatively, at a maximum pressure of 2000 psig(13,785 kPa), 1000 psig (6,890 kPa), 750 psig (5,170 kPa), 500 psig(3,450 kPa), 250 psig (1,720 kPa), 150 psig (1,030 kPa), or 100 psig(689 kPa). In an aspect, the pressure can be in a range from any minimumpressure disclosed herein to any maximum pressure disclosed herein.While not being limited thereto, the first process, second process, andthird process can be conducted and/or the second normal alpha olefin canbe formed at a reaction pressure in a range from 0 to 2000 psig (0 to13,785 kPa), from 10 to 2000 psig (69 to 13,785 kPa), from 0 to 1000psig (0 to 6,890 kPa), from 5 to 1000 psig (34 to 6,890 kPa), from 5 to750 psig (34 to 5,170 kPa), from 5 to 500 psig (34 to 3,450 kPa), from 5to 250 psig (34 to 1,720 kPa), from 5 to 150 psig (34 to 1,030 kPa), orfrom 10 to 100 psig (69 to 689 kPa). Other reaction pressure ranges arereadily apparent from this disclosure. In some aspects, the firstprocess, second process, and third process can be conducted and/or thenormal alpha olefin can be formed at atmospheric pressure, while inother aspects, the first process, second process, and third process canbe conducted and/or the normal alpha olefin can be formed atsub-atmospheric pressures. These pressure ranges also are meant toencompass circumstances where the first process, second process, andthird process are conducted and/or the normal alpha olefin is formed ata series of different pressures, instead of at a single fixed pressure,falling within the respective pressure ranges.

The first process, second process, and third process can be conducted inany suitable reactor or vessel in order to form the normal alpha olefin,non-limiting examples of which can include a fixed bed reactor, astirred tank reactor, a plug flow reactor, a loop reactor, and a tubularreactor, including more than one reactor in series or in parallel, andincluding any combination of reactor types and arrangements. The firstprocess, second process, and third process disclosed herein can be abatch process in some aspects, while in other aspects, the firstprocess, second process, and third process can be a continuous process.

Consistent with an aspect of this invention, the first process, secondprocess, and third process can be a continuous process and/or a flowprocess. For instance, the primary alcohol (or vicinal diol, or linearaldehyde)—and the acceptor—can contact a fixed bed of the catalystcomposition at any suitable weight hourly space velocity (WHSV) and atany suitable targeted single pass conversion. Moreover, in a flow orcontinuous process, multi-passes can be used to increase the overallconversion of the primary alcohol (or vicinal diol, or linear aldehyde)to the normal alpha olefin.

In an aspect, the first process, second process, and third process canbe conducted and/or the normal alpha olefin can be formed in a minimumreaction time of 5 minutes, 15 minutes, 45 minutes, or 1 hour;additionally or alternatively, in a maximum reaction time of 100 hours,75 hours, 50 hours, 24 hours, 10 hours, or 5 hours. Generally, the firstprocess, second process, and third process can be conducted and/or thenormal alpha olefin can be formed in a time period ranging from anyminimum reaction time disclosed herein to any maximum reaction timedisclosed herein. In some non-limiting aspects, the reaction time can bein a range from 5 minutes to 100 hours; alternatively, from 15 minutesto 75 hours; alternatively, from 15 minutes to 50 hours; alternatively,from 45 minutes to 75 hours; alternatively, from 45 minutes to 24 hours;alternatively, from 1 hour to 24 hours; alternatively, from 1 hour to 10hours; or alternatively, from 1 hour to 5 hours. Other reaction timesare readily apparent from this disclosure. Depending upon the processand/or type of reactor used, the minimum reaction time, maximum reactiontime, and reaction time range can be the average minimum reaction time,average maximum reaction time, and average reaction time range.

In particular aspects of this invention, the primary alcohol (or vicinaldiol, or linear aldehyde) and the catalyst composition can be contactedin the absence of a solvent. However, in other aspects, the primaryalcohol (or vicinal diol, or linear aldehyde) and the catalystcomposition can be contacted in the presence of a solvent. Typically,when used, the solvent can be present in an amount up to 1,000 wt. %,based on the weight of the primary alcohol (or vicinal diol, or linearaldehyde). Alternatively, the primary alcohol (or vicinal diol, orlinear aldehyde) and the catalyst system can be contacted in thepresence of a solvent in an amount up 750 wt. %, up to 500 wt. %, up to250 wt. %, up to 200 wt. %, up to 150 wt. %, or up to 100 wt. %. When asolvent is utilized, the minimum amount of solvent utilized can be atleast 5 wt. %, at least 10 wt. %, at least 25 wt. %, at least 50 wt. %,or at least 75 wt. %, based on the weight of the primary alcohol (orvicinal diol, or linear aldehyde). Generally, the amount of solventwhich can be utilized can range from any minimum amount of solventdisclosed herein to any maximum amount of solvent disclosed herein. Insome non-limiting aspects, the primary alcohol (or vicinal diol, orlinear aldehyde) and the catalyst system can be contacted in thepresence of a solvent in an amount of from 5 wt. % to 1,000 wt. %, from10 wt. % to 750 wt. %, from 25 wt. % to 500 wt. %, from 50 wt. % to 250wt. %, from 50 wt. % to 150 wt. %, or from 75 wt. % to 125 wt. %, basedon the weight of the primary alcohol (or vicinal diol, or linearaldehyde). Other solvent ranges are readily apparent from thisdisclosure.

As described herein, the primary alcohol (or vicinal diol, or linearaldehyde) and the catalyst composition can be contacted in the presenceof a solvent. In one aspect, the solvent can comprise, consistessentially of, or consist of, a polar solvent, while in another aspect,the solvent can comprise, consist essentially of, or consist of, ahydrocarbon, a ketone, an alcohol, an ether, or any combination thereof.Hence, mixtures and/or combinations of solvents can be utilized in thenormal alpha olefin synthesis processes disclosed herein.

In an aspect, the solvent employed in the first process, second process,and third process can comprise, consist essentially of, or consist of, ahydrocarbon solvent. Suitable hydrocarbon solvents can include, forexample, aliphatic hydrocarbons (e.g., pentane, hexane, heptane, octane,decane, and combinations thereof) and aromatic hydrocarbons (e.g.,benzene, toluene, xylene(s), ethylbenzene, and combinations thereof).

In an aspect, the solvent employed in the first process, second process,and third process can comprise, consist essentially of, or consist of, aketone, an ether, or any combination thereof alternatively, a ketone; oralternatively, an ether. Suitable ketones or ethers include C₂ to C₂₀ketones or ethers; alternatively, C₂ to C₁₀ ketones or ethers; oralternatively, C₂ to C₅ ketones or ethers. Non-limiting examples ofsuitable ketone solvents can include acetone, ethyl methyl ketone, orany combination thereof. Suitable ether solvents can be cyclic oracyclic, non-limiting examples of which can include dimethyl ether,diethyl ether, methyl ethyl ether, dibutylether, monoethers or diethersof glycols (e.g., a dimethyl glycol ether), glyme, diglyme, tetraglyme,furans, substituted furans, dihydrofuran, substituted dihydrofurans,tetrahydrofuran (THF), substituted tetrahydrofurans, tetrahydropyrans,substituted tetrahydropyrans, 1,3-dioxanes, substituted 1,3-dioxanes,1,4-dioxanes, substituted 1,4-dioxanes, or mixtures thereof. In anaspect, each substituent of a substituted furan, substituteddihydrofuran, substituted tetrahydrofuran, substituted tetrahydropyran,substituted 1,3-dioxane, or substituted 1,4-dioxane, can be a C₁ to C₅alkyl group.

Consistent with aspects of this invention, the normal alpha olefinproduct can be isolated or separated from reaction by-products, residualreactants, catalyst systems components, and the like. As would berecognized by those skilled in the art, the normal alpha olefin productcan be isolated or separated using any suitable technique, such asfiltration, evaporation, distillation, or any combination of two or moreof these techniques.

Generally, the yield of the normal alpha olefin (moles of normal alphaolefin based on the moles of the primary alcohol, vicinal diol, orlinear aldehyde) in the first process, second process, and third processcan be at least about 10%, at least about 20%, at least about 30%, atleast about 40%, or at least about 50%. In certain aspects, the presenceof an acceptor in the catalyst composition can unexpectedly anddrastically improve the yield of the normal alpha olefin, whileminimizing byproducts such as internal olefins. In such circumstances,the molar yield can be at least about 60%, at least about 70%, at leastabout 80%, at least about 90%, at least about 95%, at least about 98%,or at least about 99%. The amount of by-products, such as alkanes andinternal olefins, formed by in the first process, second process, andthird process can be less than about 20%, less than about 15%, less thanabout 10%, less than about 8%, less than about 5%, less than about 3%,less than about 2%, or less than about 1%. As above, these percentagesare molar yields based on the initial amount of the primary alcohol (orvicinal diol, or linear aldehyde).

Selective Olefin Production Using Dehydroxymethylation

Aspects of this invention are directed to processes for producing normalalpha olefins via a linear primary alcohol or terminal vicinal diol. Afourth process (a multistep normal alpha olefin synthesis) consistentwith this invention can comprise (i) conducting ahydroboration-oxidation reaction of a first normal alpha olefin havingthe structure CH₃(CH₂)_(n)HC═CH₂ to form a linear primary alcohol havingthe structure CH₃(CH₂)_(n+1)CH₂OH, and (ii) contacting the linearprimary alcohol with any catalyst composition disclosed herein (e.g.,transition metal compound, phosphine, heteroatomic acid or derivative,and acceptor) to form a second normal alpha olefin having the structureCH₃(CH₂)_(n−1)HC═CH₂ (one carbon is removed in the conversion of thefirst normal alpha olefin to the second normal alpha olefin). In thefourth process, n can be an integer ranging from 1 to 33. The fourthprocess also can be applied to a linear internal olefin, in which thedouble bond is chain-walked to the alpha position before undergoing thehydroboration-oxidation reaction. A fifth process (a multistep normalalpha olefin synthesis) consistent with this invention can comprise (i)conducting a dihydroxylation reaction of a first normal alpha olefinhaving the structure CH₃(CH₂)_(n)HC═CH₂ to form a terminal vicinal diolhaving the structure CH₃(CH₂)_(n)CH(OH)CH₂OH, and (ii) contacting theterminal vicinal diol with any catalyst composition disclosed herein toform a second normal alpha olefin having the structureCH₃(CH₂)_(n−2)HC═CH₂ (two carbons are removed in the conversion of thefirst normal alpha olefin to the second normal alpha olefin). In thefifth process, n can be an integer ranging from 2 to 33. Generally, thefeatures of the fourth process and the fifth process (e.g., the firstnormal alpha olefin, the second normal alpha olefin, the catalystcomposition, the alcohol, the diol, and the conditions under which thedehydroxymethylation reaction is conducted, among other features) areindependently described herein and these features can be combined in anycombination to further describe these two processes. Moreover,additional process steps can be performed before, during, and/or afterthe steps of these processes, unless stated otherwise.

In the fourth process and fifth process, n can be an integer that canrange from 1 to 33 and 2 to 33, respectively. In one aspect consistentwith this invention, n can be an integer from 1 to 12, from 1 to 10, orfrom 1 to 7, in the fourth process, while in another aspect, n can be aninteger from 2 to 12, from 2 to 10, or from 2 to 7, in the fifthprocess. Yet, in another aspect, n can be an integer from 3 to 10, andin still another aspect, n can be an integer from 4 to 9. For example, ncan be equal to 2, equal to 3, equal to 4, equal to 5, and so forth.Accordingly, in some aspects, the second normal alpha olefin cancomprise (or consist essentially of, or consist of) propylene, 1-butene,1-pentene, 1-hexene, 1-heptene, 1-octene, 1-nonene, 1-decene,1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene, or anycombination thereof; alternatively, 1-butene, 1-hexene, 1-octene,1-decene, 1-dodecene, or any combination thereof; alternatively,1-hexene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene, or anycombination thereof or alternatively, 1-hexene, 1-octene, 1-decene, orany combination thereof. In other aspects, the second normal alphaolefin can comprise (or consist essentially of, or consist of) 1-hexene;alternatively, 1-octene; or alternatively, 1-decene.

Referring now to step (i) of the fourth process, which is often referredto as a hydroboration-oxidation step, the process can compriseconducting a hydroboration-oxidation reaction of a first normal alphaolefin having the structure CH₃(CH₂)_(n)HC═CH₂ to form a linear primaryalcohol having the structure CH₃(CH₂)_(n+1)CH₂OH. Stated another way, inthis step, the first normal alpha olefin is subjected to ahydroboration-oxidation reaction to form a linear primary alcohol havingthe same number of carbon atoms as that of the first normal alphaolefin.

The hydroboration-oxidation step can be performed as described in U.S.Pat. Nos. 3,078,313, 3,358,034, and 3,439,046; Brown, H. C., Zweifel,G., (1959), “A Stereospecific cis Hydration of the Double Bond in CyclicDerivatives,” Journal of the American Chemical Society, 81:247; Brown,H.; Rao, B. C. (1957), “Communications—Selective Conversion of Olefinsinto Organoboranes Through Competitive Hydroboration, Isomerization andDisplacement Reactions,” Journal of Organic Chemistry, 22 (9):1137;Brewster, J. H., Negishi, E., Science 1980, 207, 44-46; Kabalka, G. W.,Hedgecock, Jr, H. C., “Mild and convenient oxidation procedure for theconversion of organoboranes to the corresponding alcohols,” J. Org.Chem. 1975, 40, 1776-1779; and Zweifel, G., Nagase, K., Brown, H. C.,“Hydroboration. XIII. The hydroboration of dienes with disiamylborane. Aconvenient procedure for the conversion of selected dienes intounsaturated alcohols,” J. Am. Chem. Soc. 1962, 84, 190-95, each of whichis incorporated herein by reference in its entirety.

Suitable hydroboration-oxidation reaction conditions to convert thefirst normal alpha olefin having the structure CH₃(CH₂)_(n)HC═CH₂ to thelinear primary alcohol having the structure CH₃(CH₂)_(n+1)CH₂OH would berecognized by those skilled in the art in view of these references andthe examples that follow.

Referring now to step (i) of the fifth process, which is often referredto as a dihydroxylation step, the process can comprise conducting adihydroxylation reaction of a first normal alpha olefin having thestructure CH₃(CH₂)_(n)HC═CH₂ to form a terminal vicinal diol having thestructure CH₃(CH₂)_(n)CH(OH)CH₂OH. Stated another way, in this step, thefirst normal alpha olefin is subjected to a dihydroxylation reaction toform a terminal vicinal diol having the same number of carbon atoms asthat of the first normal alpha olefin.

The dihydroxylation step can be performed as described in U.S. Pat. Nos.3,582,270; 5,126,494; WO 89/06225; Vanrheenen, V., Kelly, R. C., Cha, D.Y., (1976) “An improved catalytic OsO4 oxidation of olefins tocis-1,2-glycols using tertiary amine oxides as the oxidant,” TetrahedronLett. 17 (23):1973-1976; Eames, Jason, Mitchell, Helen J., Nelson, Adam,O'Brien, Peter, Warren, Stuart, Wyatt, Paul, (1999) “An efficientprotocol for Sharpless-style racemic dihydroxylation,” J. Chem. Soc.,Perkin Trans. 1, 1999 (8):1095-1104; Jacobsen, E. N., Marko, I.,Mungall, W. S., Schroeder, G., Sharpless, K. B., (1988), “Asymmetricdihydroxylation via ligand-accelerated catalysis,” J. Am. Chem. Soc. 110(6):1968-1970; Kolb, H. C., Van Nieuwenhze, M. S., Sharpless, K. B.,(1994) “Catalytic Asymmetric Dihydroxylation,” Chem. Rev. 94(8):2483-2547; Ahrgren, Leif, Sutin, Lori, “Sharpless AsymmetricDihydroxylation on an Industrial Scale,” Org. Proc. Res. Dev., 1997, 1(6), pp 425-427; and Johnson, Roy A., Sharpless, K. B., Catal.Asymmetric Synth. (1993), 227-22, each of which is incorporated hereinby reference in its entirety.

Suitable dihydroxylation reaction conditions to convert the first normalalpha olefin having the structure CH₃(CH₂)_(n)HC═CH₂ to the terminalvicinal diol having the structure CH₃(CH₂)_(n)CH(OH)CH₂OH would berecognized by those skilled in the art in view of these references andthe examples that follow.

Referring now to step (ii) of the fourth process and the fifth process,which often is referred to as the dehydroxymethylation step. In thisstep, a linear primary alcohol (or terminal vicinal diol)—such as thatformed in step (i)—can be contacted with any catalyst compositiondisclosed herein (e.g., transition metal compound, phosphine,heteroatomic acid or derivative, and acceptor) to form a second normalalpha olefin having the structure CH₃(CH₂)_(n−1)HC═CH₂ (from the linearprimary alcohol with the loss of one carbon atom) or a second normalalpha olefin having the structure CH₃(CH₂)_(n−2)HC═CH₂ (from theterminal vicinal diol with the loss of two carbon atoms).

Step (ii) of the fourth process and the fifth process can be performedin the same manner as that described above for the first process, secondprocess, and third process. Thus, any acceptor disclosed herein can beused, and the molar ratio of the acceptor to the linear alcohol (orvicinal diol) can be any amount in the range from about 0.2:1 to about1000:1. Likewise, the molar ratio of the linear alcohol (or vicinaldiol) to the transition metal of the transition metal compound or thephosphine transition metal compound complex (in the catalystcomposition) can be any molar ratio in the range from about 2:1 to about1000:1. Further, step (ii) can be performed in any solvent disclosed inrelation to the first process, the second process, and the third process(e.g., toluene, THF, dioxane), and at any temperature (e.g., from about0° C. to about 150° C.), pressure, WHSV or reaction time, and the secondnormal alpha olefin product can be isolated or separated from reactionby-products, residual reactants, catalyst systems components, and thelike using any suitable technique.

Generally, the yield of the second normal alpha olefin (moles of secondnormal alpha olefin based on the moles of the alcohol or diol) in step(ii) of the fourth process or fifth process can be at least about 10%,at least about 20%, at least about 30%, at least about 40%, or at leastabout 50%. In certain aspects, the presence of an acceptor in thecatalyst composition can unexpectedly and drastically improve the yieldof the second normal alpha olefin, while minimizing byproducts such asinternal olefins. In such circumstances, the molar yield can be at leastabout 60%, at least about 70%, at least about 80%, at least about 90%,at least about 95%, at least about 98%, or at least about 99%. Theamount of by-products, such as alkanes and internal olefins, formed instep (ii) of the fourth process and fifth process can be less than about20%, less than about 15%, less than about 10%, less than about 8%, lessthan about 5%, less than about 3%, less than about 2%, or less thanabout 1%. These percentages are molar yields based on the initial amountof the alcohol or diol.

Selective Olefin Production Using Dehydroformylation

Aspects of this invention are directed to processes for producing normalalpha olefins via a linear aldehyde. A sixth process consistent withthis invention can comprise (or consist essentially of, or consist of)(i) contacting a first normal alpha olefin having the structureCH₃(CH₂)_(n)HC═CH₂ and a metathesis catalyst system to form a linearinternal olefin having the structure CH₃(CH₂)_(n)HC═CH(CH₂)_(n)CH₃, (ii)contacting the linear internal olefin with a hydroformylation catalystsystem, carbon monoxide, and hydrogen to form a linear aldehyde havingthe formula CH₃(CH₂)_(2n+3)C(═O)H, and (iii) contacting the linearaldehyde with any catalyst composition disclosed herein (e.g.,transition metal compound, phosphine, heteroatomic acid or derivative,and acceptor) to form a second normal alpha olefin having the structureCH₃(CH₂)_(2n+1)HC═CH₂. In the sixth process, n can be an integer thatcan range from 0 to 15. Generally, the features of the sixth process(e.g., the first normal alpha olefin, the metathesis catalyst, thelinear internal olefin, the hydroformylation catalyst system, thecatalyst composition, the second normal olefin, and the conditions underwhich each of the steps are conducted, among other features) areindependently described herein and these features can be combined in anycombination to further describe the sixth normal alpha olefin synthesisprocess. Moreover, additional process steps can be performed before,during, and/or after any of the steps of any of the processes disclosedherein, unless stated otherwise.

In this multistep process, n can be an integer that can range from 0 to15. In one aspect consistent with this invention, n can be an integerfrom 0 to 10, while in another aspect, n can be an integer from 0 to 7.Yet, in another aspect, n can be an integer from 1 to 7, and in stillanother aspect, n can be an integer from 1 to 5. For example, n can beequal to 1, equal to 2, equal to 3, equal to 4, and so forth.

In some aspects of this invention, the first normal alpha olefin cancomprise, consist essentially of, or consist of, propylene, 1-butene,1-pentene, 1-hexene, 1-heptene, 1-octene, 1-nonene, 1-decene,1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene, or anycombination thereof; alternatively, 1-butene, 1-pentene, 1-hexene,1-heptene, 1-octene, or any combination thereof; or alternatively,1-butene, 1-pentene, 1-hexene, or any combination thereof. In furtheraspects, the first normal alpha olefin can comprise, consist essentiallyof, or consist of, propylene; alternatively, 1-butene; alternatively,1-pentene; alternatively, 1-hexene; alternatively, 1-heptene;alternatively, 1-octene; alternatively, 1-nonene; alternatively,1-decene; alternatively, 1-dodecene; alternatively, 1-tetradecene;alternatively, 1-hexadecene; or alternatively, 1-octadecene.

In one aspect of this invention, the first normal alpha olefin cancomprise (or consist essentially of, or consist of) 1-butene, and thesecond normal alpha olefin can comprise (or consist essentially of, orconsist of) 1-hexene. In another aspect of this invention, the firstnormal alpha olefin can comprise (or consist essentially of, or consistof) 1-pentene, and the second normal alpha olefin can comprise (orconsist essentially of, or consist of) 1-octene. In yet another aspectof this invention, the first normal alpha olefin can comprise (orconsist essentially of, or consist of) 1-hexene, and the second normalalpha olefin can comprise (or consist essentially of, or consist of)1-decene.

The integer n, the first normal alpha olefin, and the second normalalpha olefin are described herein and their features can be utilizedwithout limitation to further describe the sixth normal alpha olefinsynthesis process disclosed herein. Other suitable values for theinteger n and selections for the first normal alpha olefin and thesecond normal alpha olefin are readily apparent from this disclosure.

Step (i) of the sixth process often is referred to as the metathesisstep, and in this step, the first normal alpha olefin having thestructure CH₃(CH₂)_(n)HC═CH₂ can be contacted with a metathesis catalystsystem to form a linear internal olefin having the structureCH₃(CH₂)_(n)HC═CH(CH₂)_(n)CH₃.

Any suitable metathesis catalyst system can be used in the metathesisstep, non-limiting examples of which can include a metal oxide basedmetathesis catalyst system, a metal halide based metathesis catalystsystem, a metal carbene based metathesis catalyst system, or anycombination thereof. In one aspect, the metathesis catalyst system canbe a metal oxide based metathesis catalyst system or a metal halidebased metathesis catalyst system, while in another aspect, themetathesis system catalyst can be a metal oxide based metathesiscatalyst system; alternatively, a metal halide based metathesis catalystsystem; or alternatively, a metal carbene based metathesis catalystsystem.

Metal oxide based metathesis catalyst systems can comprise (or consistessentially of, or consist of) cobalt oxide, molybdenum oxide, tungstenoxide, rhenium oxide, or any combination thereof. For instance, themetal oxide based catalyst system can comprise (or consist essentiallyof, or consist of) cobalt oxide; alternatively, molybdenum oxide;alternatively, tungsten oxide; or alternatively, rhenium oxide.Optionally, the metal oxide based metathesis catalyst system can furthercomprise a support, or a metal alkyl activator, or both a support and ametal alkyl activator. Illustrative supports can include alumina,silica, silica-alumina, and aluminum-phosphate, amongst other solidoxide materials. Accordingly, non-limiting examples of supported metaloxide based metathesis catalyst systems can include molybdenum oxide onalumina (MoO₃/Al₂O₃), tungsten oxide on silica (WO₃/SiO₂), rhenium oxideon alumina (Re₂O₇/Al₂O₃), cobalt oxide and molybdenum oxide on alumina(CoO/MoO₃/Al₂O₃), and rhenium oxide on alumina activated withtetramethyl tin (Re₂O₇/Al₂O₃SnMe₄). Other suitable metal oxide basedmetathesis catalyst systems are known to those skilled in the art.

Further, the metal oxide based metathesis catalyst system can include ametal alkyl activator, which can include alkyl lithium, alkyl magnesium,alkyl aluminum, alkyl tin compounds, or any mixture thereof. In anaspect, the metal alkyl activator can be an alkyl lithium compound. Inanother aspect, the metal alkyl activator can be an alkyl magnesiumcompound. In another aspect, the metal alkyl activator can be an alkylaluminum compound. In yet another aspect, the metal alkyl activator canbe an alkyl tin compound. Non-limiting examples of alkyl aluminumcompounds can include trialkyl aluminum compounds and/or alkyl aluminumhalide compounds. The alkyl groups on the metal alkyl activator caninclude any C₁ to C₁₀ hydrocarbyl group, or alternatively, any C₁ to C₅hydrocarbyl group. In various aspects, the alkyl group for the metalalkyl activator can be a methyl group, ethyl group, n-propyl group,iso-propyl group, n-butyl group, sec-butyl group, or tert-butyl group;alternatively, a methyl group, ethyl group, n-butyl group, sec-butylgroup, or tert-butyl group; alternatively, a methyl group;alternatively, an ethyl group; alternatively, an n-butyl group;alternatively, a sec-butyl group; or alternatively, a tert-butyl group.Representative examples of suitable trialkyl aluminum compounds caninclude trimethylaluminum, triethylaluminum, and triisobutylaluminum.The halide of the alkyl aluminum halide compound can be chloride,bromide, or iodide; alternatively, chloride; alternatively, bromide; oralternatively, iodide. Examples of suitable alkyl aluminum halidecompounds can include ethylaluminum dichloride, diethylaluminumchloride, and ethylaluminum sesquichloride. Suitable and non-limitingexamples of alkyl tin compounds can include tetramethyl tin, tetraethyltin, and tetrabutyl tin.

Metal halide based metathesis catalyst systems can comprise (or consistessentially of, or consist of) a halide of tungsten, a halide ofmolybdenum, or a combination thereof. For instance, the metal halidebased metathesis catalyst system can comprise (or consist essentiallyof, or consist of) a halide of tungsten, or alternatively, a halide ofmolybdenum. The halide of the metal halide based metathesis catalystsystem can be chloride, bromide, or iodide. In one aspect, the halidecan be chloride, and in another aspect, the halide can be bromide, andin yet another aspect, the halide can be iodide. Hence, the metal halidebased metathesis catalyst system can comprise (or consist essentiallyof, or consist of) tungsten chloride, molybdenum chloride, or a mixturethereof; alternatively, tungsten chloride; or alternatively, molybdenumchloride.

Optionally, the metal halide based metathesis catalyst system canfurther comprise a metal alkyl activator (as described herein), oxygen,an alcohol, or any combination thereof, alternatively, a metal alkylactivator; alternatively, oxygen; or alternatively, an alcohol.Non-limiting examples of metal halide based metathesis catalyst systemscan include tungsten chloride/tetrabutyl tin (WCl₆/SnMe₄), tungstenchloride/ethylaluminum dichloride (WCl₆/EtAlCl₂), tungstenchloride/ethylaluminum dichloride/ethyl alcohol (WCl₆/EtAlCl₂/EtOH),molybdenum chloride/triethyl aluminum (MoCl₅/AlEt₃), and molybdenumchloride/triethyl aluminum/O₂ (MoCl₅/AlEt₃/O₂). Other suitable metalhalide based metathesis catalyst systems are known to those skilled inthe art.

Metal carbene based metathesis catalyst systems can comprise (or consistessentially of, or consist of) tungsten, tantalum, osmium, molybdenum,ruthenium, or any combination thereof. For instance, the metal carbenebased metathesis catalyst system can comprise (or consist essentiallyof, or consist of) tungsten; alternatively, tantalum; alternatively,osmium; alternatively, molybdenum; or alternatively, ruthenium. Thesemetal carbene based metathesis catalyst systems can contain compoundswhich have a stable metal-carbon double bond or can form a metal-carbondouble bond in situ from a metal precursor having a stable metal-carbonsingle bond.

In an aspect, a ruthenium carbene based metathesis catalyst system cancomprise a compound having the structure L¹L²X₂Ru═CHR¹, wherein L¹ andL² can be an organic ligand, X can be a halide, and R¹ can be hydrogenor a hydrocarbyl group. Generally, the compound in the ruthenium carbenebased metathesis catalyst system having the structure L¹L²X₂Ru═CHR¹ canbe described using any combination of L¹, L², X, or R¹ described herein.

Generally, L¹ and L² independently can be R′₃P, an imidazolinylidenegroup, or an imidazolidinylidene group. In some aspects, L¹ and L² canbe R′₃P; alternatively, L¹ can be R′₃P and L² can be animidazolinylidene group or an imidazolidinylidene group; alternatively,L¹ can be R′₃P and L² can be an imidazolinylidene group; alternatively,L¹ can be R′₃P and L² can be an imidazolidinylidene group;alternatively, L¹ and L² can be imidazolinylidene groups; oralternatively, L¹ and L² can be imidazolidinylidene groups. In aspectsof this invention, R′ can be a hydrocarbyl group, where each R′ of R′₃Pcan be the same; alternatively, each R′ of R′₃P can be different; oralternatively, one R′ of R′₃P can be different from the other two R′groups. In some aspects, each R′ of R′₃P independently can be a C₁ toC₁₅ hydrocarbyl group; or alternatively, a C₁ to C₁₀ hydrocarbyl group.In other aspects, each hydrocarbyl R′ of R′₃P independently can be analkyl group or an aromatic group; alternatively, an alkyl group; oralternatively, an aromatic group. In an aspect, each alkyl R′ of R′₃Pindependently can be a methyl group, ethyl group, n-propyl group,isopropyl group, tert-butyl group, neo-pentyl group, cyclopentyl group,or cyclohexyl group. In some aspects, one or more R′ groups of R′₃P canbe a phenyl group, or alternatively, a substituted phenyl group. In anaspect, the substituents of any substituted phenyl group independentlycan be a C₁-C₅ organyl group, or alternatively, a C₁-C₅ hydrocarbylgroup. In some aspects, R′₃P can be a trialkyl phosphine or triphenylphosphine; alternatively, a trialkyl phosphine; or alternatively,triphenyl phosphine. In an aspect, R′₃P can be trimethyl phosphine,triethyl phosphine, triisopropyl phosphine, tri-tert-butyl phosphine,tri-neopentyl phosphine, tricyclopentyl phosphine, tricyclohexylphosphine, or triphenyl phosphine; alternatively, triisopropylphosphine, tri-tert-butyl phosphine, tri-neopentyl phosphine,tricyclopentyl phosphine, tricyclohexyl phosphine, or triphenylphosphine; alternatively, tricyclopentyl phosphine, tricyclohexylphosphine, or triphenyl phosphine; alternatively, tricyclopentylphosphine or tricyclohexyl phosphine; alternatively, tricyclopentylphosphine; alternatively, tricyclohexyl phosphine; or alternativelytriphenyl phosphine.

In an aspect, the imidazolinylidene group or imidazolidinylidene groupcan be a C₃ to C₈₀ imidazolinylidene group or imidazolidinylidene group;alternatively, a C₃ to C₅₀ imidazolinylidene group orimidazolidinylidene group; or alternatively, a C₅ to C₄₀imidazolinylidene group or imidazolidinylidene group. In some aspects,the imidazolinylidene group can be a 1,3-disubstituted imidazolinylidenegroup. In some aspects, the imidazolidinylidene group can be a1,3-disubstituted imidazolidinylidene group. In an aspect, the1,3-substituents of the 1,3-disubstituted imidazolinylidene group or1,3-disubstituted imidazolidinylidene group independently can be anysuitable hydrocarbyl group. In an aspect, the 1,3-substituents of the1,3-disubstituted imidazolinylidene group or 1,3-disubstitutedimidazolidinylidene group independently can be a C₁ to C₃₀ hydrocarbylgroup. In some aspects, the 1,3-substituents of the 1,3-disubstitutedimidazolinylidene group or 1,3-disubstituted imidazolidinylidene groupindependently can be a C₆ to C₂₀ aromatic group or a C₁ to C₁₀ alkylgroup. In other aspects, the 1,3-substituents of the 1,3-disubstitutedimidazolinylidene group or 1,3-disubstituted imidazolidinylidene groupindependently can be a C₆ to C₂₀ aromatic group, or alternatively, a C₁to C₁₀ alkyl group. In an aspect, each aromatic group of the1,3-disubstituted imidazolinylidene group or 1,3-disubstitutedimidazolidinylidene group independently can be a substituted aromaticgroup. In some aspects, the substituted aromatic group of the1,3-disubstituted imidazolinylidene group or 1,3-disubstitutedimidazolidinylidene group can be a 2-disubstituted phenyl group, a2,6-disubstituted phenyl group, or a 2,4,6-trisubstituted phenyl group;alternatively, a 2,6-disubstituted phenyl group; or alternatively, a2,4,6-trisubstituted phenyl group. Suitable substituents for anysubstituted phenyl group within the 1,3-disubstituted imidazolinylidenegroup or 1,3-disubstituted imidazolidinylidene group can include any C₁to C₁₀ hydrocarbyl group, or alternatively, any C₁ to C₅ hydrocarbylgroup. In some aspects, each hydrocarbyl substituent independently canbe a methyl group, ethyl group, n-propyl group, iso-propyl group,n-butyl group, sec-butyl group, or tert-butyl group; alternatively, amethyl group, ethyl group, n-butyl group, sec-butyl group, or tert-butylgroup; alternatively, a methyl group; alternatively, an ethyl group,alternatively, an isopropyl group; or alternatively, a tert-butyl group.In some aspects, each substituted aromatic group of the1,3-disubstituted imidazolinylidene group or 1,3-disubstitutedimidazolidinylidene group independently can be a 2,6-diisopropylphenylgroup or a 2,4,6-trimethylphenyl group; alternatively, a2,6-diisopropylphenyl group; or alternatively, a 2,4,6-trimethylphenylgroup.

In various aspects, each X of the compound having the structureL¹L²X₂Ru═CHR¹ independently can be chloride, bromide, or iodide. In anaspect, X can be chloride. In another aspect, X can be bromide. In yetanother aspect, X can be iodide. R¹ of the compound having the structureL¹L²X₂Ru═CHR¹ can be hydrogen or a C₁ to C₂₀ hydrocarbyl group. In someaspects, R¹ can be a methyl group, an ethyl group, an isopropyl group, atert-butyl group, a phenyl group, a 2-methyl-2-propene group, or a2,2-diphenylethene group. In other aspects, R¹ can be a tert-butylgroup, a phenyl group, a 2-methyl-2-propene group, or a2,2-diphenylethene group; alternatively, hydrogen; alternatively, atert-butyl group; alternatively, a phenyl group; alternatively, atert-butyl group; alternatively, a phenyl group; alternatively, a2-methyl-2-propene group; or alternatively, a 2,2-diphenylethene group.

In some non-limiting aspects, the ruthenium carbene based metathesiscatalyst system can comprise dichloro(phenylmethylene) bis(tricyclohexylphosphine) ruthenium, dichloro(3-methyl-2-butenylidene)bis(tricyclohexyl phosphine) ruthenium,dichloro(3-methyl-2-butenylidene) bis(tricyclopentyl phosphine)ruthenium,1,3-bis-(2,4,6-trimethylphenyl)-2-(imidazolidinylidene)(phenylmethylene)dichloro(tricyclohexylphosphine) ruthenium, or1,3-bis-(2,6-diisopropy1phenyl)-2-(imidazolidinydene)(phenylmethylene)dichloro(tricyclohexylphosphine) ruthenium. In some aspects, the ruthenium carbene basedmetathesis catalyst system can comprise dichloro(phenylmethylene)bis(tricyclohexyl phosphine) ruthenium; alternatively,dichloro(3-methyl-2-butenylidene) bis(tricyclohexyl phosphine)ruthenium; alternatively,1,3-bis-(2,4,6-trimethylphenyl)-2-(imidazolidinylidene)(phenylmethylene)dichloro(tricyclohexylphosphine) ruthenium; or alternatively,1,3-bis-(2,6-diisopropylphenyl)-2-(imidazolidinylidene)(phenylmethylene)dichloro(tricyclohexylphosphine) ruthenium.

In an aspect, a molybdenum carbene based metathesis catalyst system cancomprise a compound having the structure Mo(═CHR²)(NAr)(OR³)₂, whereinR² is a hydrogen or hydrocarbyl group, Ar is a substituted aromaticring, and R³ is a hydrocarbyl group or a halogenated hydrocarbyl group.Generally, the compound in the molybdenum carbene based metathesiscatalyst system having the structure Mo(═CHR²)(NAr)(OR³)₂ can bedescribed using any combination of R², Ar, and R³ described herein.

In some aspects, R² of the compound having the structureMo(═CHR²)(NAr)(OR³)₂ can be hydrogen or a C₁ to C₂₀ hydrocarbyl group,or alternatively, a C₁ to C₂₀ hydrocarbyl group. In some aspects, R² canbe a methyl group, an ethyl group, an isopropyl group, a tert-butylgroup, a phenyl group, a 2-methyl-2-propene group, or a2,2-diphenylethene group. In other aspects, R² can be a tert-butylgroup, a phenyl group, a 2-methyl-2-propene group, or a2,2-diphenylethene group; alternatively, a tert-butyl group or a phenylgroup; alternatively, hydrogen; alternatively, a tert-butyl group;alternatively, a phenyl group; alternatively, a 2-methyl-2-propenegroup; or alternatively, a 2,2-diphenylethene group.

In an aspect, the substituted aromatic ring, Ar, of the compound havingthe structure Mo(═CHR²)(NAr)(OR³)₂ can be a C₆ to C₃₀ aromatic group, oralternatively, a C₆ to C₂₀ aromatic group. In some aspects, eachsubstituent of the substituted aromatic ring, Ar, independently can be aC₆ to C₂₀ hydrocarbyl group, a C₁ to C₁₀ hydrocarbyl group, or a C₁ toC₅ hydrocarbyl group. In some aspects, the substituted aromatic ring,Ar, can be a 2-substituted phenyl group, a 2,6-disubstituted phenylgroup, or a 2,4,6-trisubstituted phenyl group. In an aspect, eachsubstituent of the substituted aromatic ring independently can be amethyl group, an ethyl group, an isopropyl group, a tert-butyl group, ora neopentyl group; alternatively, a methyl group, an isopropyl group, ora tert-butyl group; alternatively, a methyl group or an isopropyl group.In some aspects, each substituent of the substituted aromatic ringindependently can be a methyl group; alternatively, an isopropyl group;or alternatively, a tert-butyl group. In some non-limiting aspects, thesubstituted aromatic ring, Ar, can be a 2-tert-butylphenyl group, a2,6-dimethylphenyl group, a 2,6-diisopropylphenyl group, or a2,4,6-trimethyl phenyl group; alternatively, a 2-tert-butylphenyl group;alternatively, a 2,6-dimethylphenyl group; alternatively, a2,6-diisopropylphenyl group; or alternatively, a 2,4,6-trimethyl phenylgroup.

In an aspect, each R³ of the compound having the structureMo(═CHR²)(NAr)(OR³)₂ independently can be a C₁ to C₁₀ organic group, oralternatively, a C₁ to C₅ organic group. In some aspects, the C₁ to C₁₀or C₁ to C₅ organic group can be a hydrocarbylhalyl group (a groupconsisting of hydrogen, carbon, and halogen atoms); alternatively, ahydrocarbylfluoryl group (a group consisting of hydrogen, carbon, andfluorine atoms); or alternatively, a hydrocarbyl group. In an aspect,the halogen atoms of the hydrocarbylhalyl group can be fluorine,chlorine, bromine, iodine, or any combination thereof; alternatively,fluorine; alternatively, chlorine; alternatively, bromine; oralternatively, iodine. In some aspects, each R³ independently can be atert-butyl group or a hexafluoro-tert-butyl group. In other aspects,(OR³)₂ can represent a single organic group wherein the two R³ groupsattached to the oxygen atoms are connected via a bond between anydivalent, trivalent, or tetravalent atom within the R³ groups. Infurther aspects, (OR³)₂ can represent a single organic group wherein thetwo R³ groups attached to the oxygen atoms are connected via acarbon-carbon bond between any carbon atom of the two R³ groups.

In an aspect, the molybdenum carbene based metathesis catalyst systemcan comprise Mo(═CH—C(CH₃)₃)(N-2,6-diisopropylphenyl)(OC(CH₃)₃),Mo(═CH—C(CH₃)₂(C₆H₅))(N-2,6-diisopropylphenyl)(OC(CH₃)₃),Mo(═CH—C(CH₃)₃)(N-2,6-diisopropylphenyl)-(OC(CH₃)(CF₃)₂), orMo(═CH—C(CH₃)₂(C₆H₅))(N-2,6-diisopropylphenyl)(OC(CH₃)(CF₃)₂). In otheraspects, the molybdenum carbene based metathesis catalyst system cancomprise Mo(═CH—C(CH₃)₃)(N-2,6-diisopropylphenyl)(OC(CH₃)₃);alternatively, Mo(═CH—C(CH₃)₂(C₆H₅))(N-2,6-diisopropylphenyl)(OC(CH₃)₃);alternatively, Mo(═CH—C(CH₃)₃)(N-2,6-diisopropylphenyl)(OC(CH₃)(CF₃)₂);or alternatively,Mo(═CH—C(CH₃)₂(C₆H₅))(N-2,6-diisopropylphenyl)(OC(CH₃)(CF₃)₂).

Optionally, the metal carbene based metathesis catalyst system canfurther comprise a support. Illustrative supports can include alumina,silica, silica-alumina, and aluminum-phosphate, amongst other solidoxide materials. Additionally, the support can comprise a polymer, andthe metal carbene metathesis catalyst compound can be tethered to thesupport via any of the ligands which do not contain the metal-carbondouble bond.

Any suitable conditions for the metathesis step can be employed, aswould be recognized by those skilled in the art in view of thisdisclosure and the examples that follow, and U.S. Pat. No. 8,765,984.

Referring now to step (ii) of the sixth process, which often is referredto as the hydroformylation step. In this step, a linear internalolefin—such as that formed in the metathesis step—can be contacted witha hydroformylation catalyst system, carbon monoxide, and hydrogen toform a linear aldehyde having the formula CH₃(CH₂)_(2n+3)C(═O)H. Asdescribed herein, n can be an integer ranging from 0 to 15; for example,n can be an integer from 0 to 10, n can be an integer from 0 to 7, n canbe an integer from 1 to 7, or n can be an integer from 1 to 5.

Consistent with certain aspects of this invention, step (ii) cancomprise contacting the linear internal olefin with a hydroformylationcatalyst system and syngas (also referred to as synthesis gas) to formthe linear aldehyde. As would be recognized by those skilled in the art,syngas is a mixture containing predominately carbon monoxide andhydrogen. Syngas also can contain carbon dioxide and methane in lesseramounts.

Any suitable hydroformylation catalyst system can be used in thehydroformylation step, non-limiting examples of which can include arhodium compound, a cobalt compound, a ruthenium compound, an iridiumcompound, a platinum compound, a palladium compound, an iron compound,or any combination thereof. For instance, the hydroformylation catalystsystem can comprise a rhodium compound; alternatively, a cobaltcompound; alternatively, a ruthenium compound; alternatively, an iridiumcompound; alternatively, a platinum compound; alternatively, a palladiumcompound; or alternatively, an iron compound.

Any suitable conditions for the hydroformylation step can be employed,as would be recognized by those skilled in the art in view of thisdisclosure, and in particular, the examples that follow.

Referring now to step (iii) of the sixth process, which often isreferred to as the dehydroformylation step. In this step, a linearaldehyde—such as that formed in the hydroformylation step—can becontacted with any catalyst composition disclosed herein (e.g.,transition metal compound, phosphine, heteroatomic acid or derivative,and acceptor) to form a second normal alpha olefin having the structureCH₃(CH₂)_(2n+1)HC═CH₂. In this process, n can be an integer ranging from0 to 15; for example, n can be an integer from 0 to 10, n can be aninteger from 0 to 7, n can be an integer from 1 to 7, or n can be aninteger from 1 to 5. Accordingly, in some aspects, the second normalalpha olefin can comprise (or consist essentially of, or consist of)ethylene, propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene,1-nonene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene,1-octadecene, or any combination thereof; alternatively, 1-butene,1-hexene, 1-octene, 1-decene, 1-dodecene, or any combination thereof;alternatively, 1-hexene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene,or any combination thereof; or alternatively, 1-hexene, 1-octene,1-decene, or any combination thereof. In other aspects, the secondnormal alpha olefin can comprise (or consist essentially of, or consistof) 1-hexene; alternatively, 1-octene; or alternatively, 1-decene.

Step (iii) of the sixth process can be performed in the same manner asthat described above for the first process, second process, and thirdprocess. Thus, any acceptor disclosed herein can be used, and the molarratio of the acceptor to the linear aldehyde can be any amount in therange from about 0.2:1 to about 1000:1. Likewise, the molar ratio of thelinear aldehyde to the transition metal of the transition metal compoundor the phosphine transition metal compound complex (in the catalystcomposition) can be any molar ratio in the range from about 2:1 to about1000:1. Further, step (iii) can be performed in any solvent disclosed inrelation to the first process, the second process, and the third process(e.g., toluene, THF, dioxane) and at any temperature (e.g., from about0° C. to about 150° C.), pressure, WHSV or reaction time, and further,the second normal alpha olefin product can be isolated or separated fromreaction by-products, residual reactants, catalyst systems components,and the like, using any suitable technique.

Generally, the yield of the second normal alpha olefin (moles of secondnormal alpha olefin based on the moles of the linear aldehyde) in step(iii) of this multistep process can be at least about 10%, at leastabout 20%, at least about 30%, at least about 40%, or at least about50%. In certain aspects, the presence of an acceptor in the catalystcomposition can unexpectedly and drastically improve the yield of thesecond normal alpha olefin, while minimizing byproducts such as internalolefins. In such circumstances, the molar yield can be at least about60%, at least about 70%, at least about 80%, at least about 90%, atleast about 95%, at least about 98%, or at least about 99%. The amountof by-products, such as alkanes and internal olefins, formed in step(iii) of the multistep process can be less than about 20%, less thanabout 15%, less than about 10%, less than about 8%, less than about 5%,less than about 3%, less than about 2%, or less than about 1%. Thesepercentages are molar yields based on the initial amount of the linearaldehyde).

In another aspect of this invention, a seventh process for producing anormal alpha olefin is provided, and in this aspect, the process cancomprise (or consist essentially of, or consist of) (a) contacting alinear internal olefin having the structureCH₃(CH₂)_(p)HC═CH(CH₂)_(q)CH₃ with a hydroformylation catalyst system,carbon monoxide, and hydrogen to form a linear aldehyde having theformula CH₃(CH₂)_(p+q+3)C(═O)H, and (b) contacting the linear aldehydewith any catalyst composition disclosed herein (e.g., transition metalcompound, phosphine, heteroatomic acid or derivative, and acceptor) toform a normal alpha olefin having the structure CH₃(CH₂)_(p+q+1)HC═CH₂.In the seventh process, p and q can be integers that independently canrange from 0 to 15. In this process, p and q can be the same ordifferent; alternatively, the same; or alternatively, different.Generally, the features of the seventh process (e.g., the linearinternal olefin, the hydroformylation catalyst system, the linearaldehyde, the catalyst composition, the normal alpha olefin, and theconditions under which each of the steps are conducted, among otherfeatures) are independently described herein and these features can becombined in any combination to further describe the seventh normal alphaolefin synthesis process. Moreover, additional process steps can beperformed before, during, and/or after any of the steps of any of theprocesses disclosed herein, unless stated otherwise.

For instance, the internal olefin having the formulaCH₃(CH₂)_(p)HC═CH(CH₂)_(q)CH₃ can be produced by any method known tothose having ordinary skill in the art. In an aspect, the linearinternal olefin having the structure CH₃(CH₂)_(p)HC═CH(CH₂)_(q)CH₃ canbe produced by the metathesis of an alpha olefin having the formulaCH₃(CH₂)_(p)HC═CH₂ and an alpha olefin having the formulaCH₃(CH₂)_(q)HC═CH₂: e.g., the process for producing a normal alphaolefin can further comprise a step of contacting a normal alpha olefinhaving the structure CH₃(CH₂)_(p)HC═CH₂, a normal alpha olefin havingthe formula CH₃(CH₂)_(q)HC═CH₂, and a metathesis catalyst system to formthe linear internal olefin having the structureCH₃(CH₂)_(p)HC═CH(CH₂)_(q)CH₃. In another aspect, the linear internalolefin having the structure CH₃(CH₂)_(p)HC═CH(CH₂)_(q)CH₃ can beproduced by the dehydrogenation of a linear alkane having the formulaCH₃(CH₂)_(p+q+2)CH₃.

In the seventh process, step (a) is often referred to as thehydroformylation step, and step (a) can have any of the features andattributes (e.g., the hydroformylation catalyst system) as thatdescribed herein for hydroformylation step (ii) in the sixth process.Likewise, step (b) of the seventh process is often referred to as thedehydroformylation step, and step (b) can have any of the feature orattributes as that described herein for the first process, the secondprocess, and the third process: the acceptor, the catalyst composition,the molar ratio of the acceptor to the linear aldehyde, the molar ratioof the linear aldehyde to the transition metal, the solvent, thereaction temperature, the reaction pressure, the WHSV or reaction time,and the yield of the normal alpha olefin (moles of normal alpha olefinbased on the moles of the linear aldehyde), among others.

In this normal alpha olefin synthesis process, p and q independently canbe integers that range from 0 to 15. In one aspect consistent with thisinvention, p and q independently can be an integer from 0 to 10, whilein another aspect, p and q independently can be an integer from 0 to 7.Yet, in another aspect, p and q independently can be an integer from 1to 7, and in still another aspect, p and q independently can be aninteger from 1 to 5. For example, p and q independently can be equal to1, equal to 2, equal to 3, or equal to 4.

The normal alpha olefin produced in this process, having the structureCH₃(CH₂)_(p+q+1)HC═CH₂, is not particularly limited. However, in oneaspect of this invention, the normal alpha olefin can comprise, consistessentially of, or consist of, ethylene, propylene, 1-butene, 1-pentene,1-hexene, 1-heptene, 1-octene, 1-nonene, 1-decene, 1-dodecene,1-tetradecene, 1-hexadecene, 1-octadecene, or any combination thereof;alternatively, 1-butene, 1-hexene, 1-octene, 1-decene, 1-dodecene, orany combination thereof; alternatively, 1-butene, 1-hexene, 1-octene,1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene, or anycombination thereof; alternatively, 1-hexene, 1-octene, 1-decene,1-dodecene, 1-tetradecene, or any combination thereof; or alternatively,1-hexene, 1-octene, 1-decene, or any combination thereof. In anotheraspect, the normal alpha olefin can comprise, consist essentially of, orconsist of, 1-butene; alternatively, 1-hexene; alternatively, 1-octene;alternatively, 1-decene; alternatively, 1-dodecene; alternatively,1-tetradecene; alternatively, 1-hexadecene; or alternatively,1-octadecene. In yet another aspect, the normal alpha olefin cancomprise, consist essentially of, or consist of, 1-hexene, 1-octene,1-decene, or any combination thereof.

The integer p, the integer q, and the normal alpha olefin are describedherein and their features can be utilized without limitation to furtherdescribe the seventh normal alpha olefin synthesis process disclosedherein. Other suitable values for the integer p and the integer q, andselections for the normal alpha olefin, are readily apparent from thisdisclosure.

In an aspect, wherein the linear internal olefin is produced viametathesis, 1) the normal alpha olefin having the structureCH₃(CH₂)_(p)HC═CH₂ can be propene, 2) the normal alpha olefin having theformula CH₃(CH₂)_(q)HC═CH₂ can be pentene, 3) the linear internal olefincan be a linear internal butene, a linear internal hexene, a linearinternal octene, or any combination thereof, and 4) the normal alphaolefin having the structure CH₃(CH₂)_(p+q+1)HC═CH₂ can be 1-butene,1-hexene, 1-octene, or any combination thereof, or alternatively, 1) thenormal alpha olefin having the structure CH₃(CH₂)_(p)HC═CH₂ can bepropene, 2) the normal alpha olefin having the formulaCH₃(CH₂)_(q)HC═CH₂ can be heptene, 3) the linear internal olefin can bea linear internal butene, a linear internal octene, a linear internaldodecene, or any combination thereof, and 4) the normal alpha olefinhaving the structure CH₃(CH₂)_(p+q+1)HC═CH₂ can be 1-butene, 1-octene,1-dodecene, or any combination thereof. In some aspects, wherein thelinear internal olefin is produce via metathesis, 1) the normal alphaolefin having the structure CH₃(CH₂)_(p)HC═CH₂ can be butene, 2) thenormal alpha olefin having the formula CH₃(CH₂)_(q)HC═CH₂ can be hexene,3) the linear internal olefin can be a linear internal hexene, a linearinternal octene, a linear internal decene, or any combination thereof,and 4) the normal alpha olefin having the structureCH₃(CH₂)_(p+q+1)HC═CH₂ can be 1-hexene, 1-octene, 1-decene, or anycombination thereof; or alternatively, 1) the normal alpha olefin havingthe structure CH₃(CH₂)_(p)HC═CH₂ can be butene, 2) the normal alphaolefin having the formula CH₃(CH₂)_(q)HC═CH₂ can be octene, 3) thelinear internal olefin can be a linear internal hexene, a linearinternal decene, a linear internal tetradecene, or any combinationthereof, and 4) the normal alpha olefin having the structureCH₃(CH₂)_(p+q+1)HC═CH₂ can be 1-hexene, 1-decene, 1-tetradecene, or anycombination thereof. In other aspects, wherein the linear internalolefin is produce via metathesis, 1) the normal alpha olefin having thestructure CH₃(CH₂)_(p)HC═CH₂ can be pentene, 2) the normal alpha olefinhaving the formula CH₃(CH₂)_(q)HC═CH₂ can be heptene, 3) the linearinternal olefin can be a linear internal octene, a linear internaldecene, a linear internal dodecene, or any combination thereof, and 4)the normal alpha olefin having the structure CH₃(CH₂)_(p+q+1)HC═CH₂ canbe 1-octene, 1-decene, 1-dodecene, or any combination thereof. Othercombinations of 1) a normal alpha olefin having the structureCH₃(CH₂)_(p)HC═CH₂, 2) a normal alpha olefin having the formulaCH₃(CH₂)_(q)HC═CH₂, 3) a linear internal olefin, and 4) a normal alphaolefin having the structure CH₃(CH₂)_(p+q+1)HC═CH₂ are readily apparentfrom this disclosure.

EXAMPLES

The invention is further illustrated by the following examples, whichare not to be construed in any way as imposing limitations to the scopeof this invention. Various other aspects, modifications, and equivalentsthereof which, after reading the description herein, can suggestthemselves to one of ordinary skill in the art without departing fromthe spirit of the present invention or the scope of the appended claims.

Example 1 Reaction of 1-Dodecanol Without an Acceptor

Example 1 was conducted by combining 1-dodecanol (0.2 mmol),[Rh(cod)OMe]₂ (2 mol %), 3-OMeBzOH (4 mol %), and Xantphos (4 mol %) in0.4 mL toluene and heating the solution to 90° C. (see reaction schemebelow). The reaction continued for 24 h before analyzing the crudereaction mixture by gas chromatography using durene as an internalstandard to determine the amount of 1-undecene, 1-undecane, and undeceneisomers present in the reaction mixture. Gas chromatography analysisdetermined that only 1-undecane was present in the reaction mixture (10mol % yield).

Examples 1A-1K Reaction of 1-Dodecanol in the Presence of VariousAcceptors

Examples 1A-1K utilized the general experimental procedure describedabove for Example 1, except that an acceptor (3 molar equivalents basedon the primary alcohol) was used. Examples 1A-1K were conducted assingle, individual experiments; results from each reaction are shown inTable 1 below. Surprisingly, Example 1K, which employeddimethylacrylamide as the acceptor, exhibited a dramatic and unexpectedimprovement to the selectivity of the reaction with respect to theC_((n−)) olefin product, producing a 95% molar yield of the desired1-undecene product, and only about 3 mol % of alkane and internal olefinbyproducts. Moreover, Examples 1H-1J also demonstrated excellentselectivity, each having a yield of 1-undecene above 30%, using ethylacrylate, t-butyl acrylate, and acrylamide, respectively.

TABLE 1 Example Acceptor 1-undecene 1-undecane Isomers 1A

32 — 2 1B

18 — 8 1C

— 15 — 1D

— 30 — 1E

— 12 — 1F

10  7 2 1G

 3  9 — 1H

33  1 1 1I

41  2 1 1J

35  2 1 1K

95  1 2

Examples 2A-2T Reaction of Various Primary Alcohol Compounds UsingDimethylacrylamide as the Acceptor

Examples 2A-2T utilized the general experimental procedure describedabove for Inventive Example 1K (dimethylacrylamide), except that theprimary alcohol compound reactant was substituted as indicated in thechart below; and except that 2H used 6 molar equivalents ofdimethylacrylamide to account for the dual primary alcohol groupspresent in the starting material. The compounds shown below representthe primary alcohol compound and olefin product superimposed over thesame structure; the dashed bonds represent the carbon-carbon bond brokenduring the reaction. Surprisingly, the oxidative dehydroxymethylationprocesses demonstrated a molar yield of the expected olefin in a rangefrom 75% to 95%. Thus, the reaction is shown to be incredibly robustacross compounds having protected groups (2L-2T) or additionalfunctional groups comprising a π-bond present in the compound (2B-2G).

Examples 3A-3C Reaction of Allylic Alcohols

Examples 3A-3C utilized the general experimental procedure describedabove for Inventive Example 1K (dimethylacrylamide), except that theprimary alcohol compound reactant was substituted as indicated in thescheme below and only 1.5 equivalents of dimethylacrylamide were used.Surprisingly, the terminal olefin was produced in high yield, andwithout significant byproducts.

Example 4 Oxidative Dehydroformylation of an Aldehyde Compound

Example 4 utilized the general experimental procedure described abovefor Inventive Examples 3A-3C, except that the primary alcohol compoundreactant was substituted for aldehyde compound 4, and the amount of[Rh(cod)OMe]₂ (0.5 mol %), 3-OMeBzOH (1 mol %), and Xantphos (1 mol %)were reduced, and the reaction time was only 3 h. Surprisingly, theα-olefin product was formed in 94% yield in only 3 h, even though acomparatively small amount of the catalyst composition was used in thereaction.

Examples 5A-5B Dehomologations of Olefin Feedstocks

Examples 5A-5B represent a synthetic pathway to one-carbon andtwo-carbon dehomologations of a common olefin feedstock, 1-dodecene(reaction schemes below).

In Example 5A, 1-dodecene was subjected to a two-step synthesisincluding (i) hydroboration-oxidation of 1-dodecene by establishedmethods to yield 1-dodecanol, and (ii) oxidative dehydroxymethylation of1-dodecanol according to the general experimental procedure describedabove for Inventive Example 1K. The two-step process yielded the C₁₁α-olefin in excellent yield (86%).

In Example 5B, 1-dodecene was subjected to a two-step process including(i) olefin dihydroxylation of 1-dodecene by established methods to yield1,2-dodecanediol, and (ii) successive oxidative dehydroxymethylations of1,2-dodecanediol according to the general experimental proceduredescribed above for Inventive Example 1K, using twice the amount ofsacrificial acceptor (4 molar equivalents) to account for the removal ofan additional hydroxyl group (as in Example 2H). The two-step processyielded the C₁₀ α-olefin in good yield (75%).

Examples 6A-6C Natural Product Synthesis

Examples 6A-6C demonstrate the utility of the oxidativedehydroxymethylation processes disclosed herein for the synthesis ofcomplex structures and in the presence of benzyl protecting groups orsecondary hydroxyl groups. Each of Examples 6A-6C underwent oxidativedehydroxymethylation according to the general experimental proceduredescribed above for Inventive Example 1K.

Example 6A provides an example of oxidative dehydroxymethylationperformed in the presence of protected alcohol groups. Surprisingly, nodebenzylation was observed, and the α-olefin product was formed in goodyield.

Example 6B demonstrates oxidative dehydroxymethylation of a compoundcontaining two unprotected secondary alcohol functional groups: onesterically accessible and one sterically hindered. Surprisingly, thesterically hindered secondary hydroxyl group was unaffected by thereaction. Further, the sterically accessible secondary hydroxyl groupwas converted to a ketone, and no further conversion of the ketone to analkene was observed.

Example 6C takes advantage of the chemoselectivity demonstrated inExample 6B to provide a synthetic route to (+)-yohimbenone fromyohimbenol in a single step. As shown below, the primary alcohol isconverted to a Michael acceptor in good yield, despite the product beingavailable as a potential sacrificial acceptor as the reactionprogresses.

Constructive Example 7

Constructive Example 7 demonstrates the conversion of 1-hexene to1-decene via a metathesis (homogeneous), isomerization-hydroformylation(un-ligated), and dehydroformylation pathway as shown in the synthesisscheme below (where n=3).

The reaction scheme for the homogeneous metathesis step is shown below.

The metathesis step can be performed as follows. In a drybox under an N₂atmosphere, a 500 mL round bottom flask with a magnetic stir bar ischarged with 1-hexene (250 mL, 168 g, ˜2 mol). The flask is placed in analuminum block on a temperature controlled heating plate at ˜50° C. andallowed to equilibrate temperature. To this stirring solution, a Grubbs2^(nd) Generation Catalyst (dichloro[1,3-bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene] (benzylidene)(tricyclohexylphosphine) ruthenium(II), 4.2 mg, 4.9 μmol) is added toinitiate the reaction. Reaction progress can be monitored by takingaliquot samples and analyzing them by GC-FID for reaction equilibrium,which typically takes 4-8 hr. Any produced ethylene is allowed to bubbleand leave the flask as it is not capped in the glovebox. Upon completionof the reaction, the solution is cooled, filtered, and the reactioncontents distilled to isolate 5-decene. The reaction yield is ˜40-50%5-decene by fractional distillation.

The reaction scheme for the isomerization-hydroformylation (un-ligated)step is shown below.

The isomerization-hydroformylation step can be performed as follows. A 5L continuously stirred autoclave is charged with 190 g (1 mol) of5-decene in 3.8 L of benzene and 4.27 g (0.0125 mol) of recentlysublimed Co₂(CO)₈. The decene:cobalt molar ratio is maintained at ˜40:1.The autoclave is pressurized with 3000 psig of a 1:1 mix of Syn-Gasmixture (CO:H₂) that is fed on demand and is heated at 120° C. until thereaction reaches 40-60% conversion, as monitored by aliquot sampling andGC-FID analysis. GC-FID reveals that, upon analysis of the reaction,greater than 50% of the internal olefin is converted to the primaryaldehyde, 1-undecanal. The remainder of the product is a mixture of thevarious internal aldehydes declining in yield from the primary position.The products then can be individually isolated by fractionaldistillation to yield 90+% pure 1-undecanal.

The reaction scheme for the dehydroformylation step is shown below.

The dehydroformylation step to produce 1-decene can be performed asfollows. In a drybox under an N₂ atmosphere, a 500 mL round bottom flaskwith a magnetic stir bar is charged with [(COD)RhOCH₃]₂ (2.72 g, 5mmol), xantphos (5.79 g, 10 mmol), 3-methoxybenzoate (1.52 g, 10 mmol),1-undecanal (170 g, 1 mol), and 250 mL (˜3 mol) of THF. Norbornadiene(111 g, 1.2 mol) is then added last to the reaction mixture. The flaskis placed in an aluminum block on a temperature controlled heating platefor 24 hr at 60° C. Reaction progress is monitored by taking aliquotsamples and analyzing via GC-FID. Upon completion of the reaction, thereaction mixture is cooled, filtered, and the reaction product isdistilled to isolate decene by fractional distillation. Product yield is90+% decenes in a 95:5 ratio of 1-decene:2-decene, as determined byGC-FID.

Constructive Example 8

Constructive Example 8 demonstrates the conversion of 1-hexene to1-decene via a metathesis (heterogeneous),isomerization-hydroformylation (ligated), and dehydroformylation pathwayas shown in the synthesis scheme below (where n=3).

The reaction scheme for the heterogeneous metathesis step is shownbelow.

The metathesis step can be performed as follows. A 4-inch I.D. by 5-footlong stainless steel pipe is heated electrically for controlling reactortemperature and for catalyst activation/regeneration. The reactorcontains 8.2 kg of molybdenum oxide-on-alumina catalyst (1.3% Mo0₃,0.07% SiO₂) from Nalco Chemical Company, consisting of ⅛″ extrudatepellets treated with 1.5 wt. % KOH. The catalyst is regenerated by“burning off” polymer and hydrocarbons, and holding the catalyst for 6hr at 565° C. under air. The catalyst temperature is then reduced andthe atmosphere changed to N₂. 1-hexene is distilled prior to use andcharged to an olefin feed vessel. From the feed vessel, the 1-hexene ispumped at constant rate upflow through the catalyst bed. Reactionconditions are typically 87-110° C., at 20 psig pressure, with an LHSVof 0.5. The product then can be flowed into a product hold vessel, whereethylene is allowed to be flashed overhead. The crude product is thensent to a kettle bottom of a distillation column and distilled until theconcentration of 5-decene in the kettle bottom reaches ˜80%. At thispoint, approximately, 20 L of crude kettle product is obtained. Thecrude kettle product, approximately 73 kg, is loaded into the kettle ofa 2″ stainless steel distillation column with ¼″ Octapac and distilledwith 5-decene coming as the last cut at 86-89° C. at 50 mm Hg to yieldapproximately 41 kg of 5-decene with the following estimatedspecifications:

Purity (wt. %) 99.6 cis 5-decene (wt. %) 18.1 trans 5-decene (wt. %)81.5 Specific gravity (20/20° C.) 0.742 Refractive index (N_(D) ²⁰ )1.428 Freezing point (° C.) −75.8 Boiling point (° C.) 169.8

The reaction scheme for the isomerization-hydroformylation (ligated)step is shown below.

The isomerization-hydroformylation step can be performed as follows. A 1L continuously stirred autoclave is charged with 600 mL of a 1.68 Msolution of 5-decene (˜190 g, 1 mol) in toluene, 0.2 g (0.63 mmol) of[Rh(acac)(COD)], and 5.8 g (6.4 mmol) of3-aryloxy-1,3,2-dioxaphosphine-4-ones ligand, P-Ligand. The autoclave ispressurized with 300 psig of a 1:1 mix of syngas mixture (CO:H₂) that isfed on demand and is heated at 130° C. for 3 hr. GC-FID reveals that,upon analysis of the reaction, greater than 65% of the internal olefinis converted to the primary aldehyde, 1-undecanal. The remainder of theproduct is a mixture of the various internal aldehydes declining inyield from the primary position. The products then can be individuallyisolated by fractional distillation to yield 90+% pure 1-undecanal.

The reaction scheme for the dehydroformylation step is shown below.

The dehydroformylation step to produce 1-decene can be performed asfollows. In a drybox under an N₂ atmosphere, a 500 mL round bottom flaskwith a magnetic stir bar is charged with [(COD)RhOCH₃]₂ (2.72 g, 5mmol), xantphos (5.79 g, 10 mmol), 3-methoxybenzoate (1.52 g, 10 mmol),1-undecanal (170 g, 1 mol), and 250 mL (˜3 mol) of THF. Norbornadiene(111 g, 1.2 mol) is then added last to the reaction mixture. The flaskis placed in an aluminum block on a temperature controlled heating platefor 24 hr at 60° C. Reaction progress is monitored by taking aliquotsamples and analyzing via GC-FID. Upon completion of the reaction, thereaction mixture is cooled, filtered, and the reaction product isdistilled to isolate decene by fractional distillation. Product yield is90+% decenes in a 95:5 ratio of 1-decene:2-decene, as determined byGC-FID.

The invention is described herein with reference to numerous aspects andspecific examples. Many variations will suggest themselves to thoseskilled in the art in light of the detailed description. All suchobvious variations are within the full intended scope of the appendedclaims. Other aspects of the invention can include, but are not limitedto, the following (aspects are described as “comprising” but,alternatively, can “consist essentially of” or “consist of”):

Aspect 1. A catalyst composition comprising:

(I) a transition metal compound, a phosphine, and a heteroatomic acid orheteroatomic acid derivative, or (II) a phosphine transition metalcompound complex and a heteroatomic acid or heteroatomic acidderivative.

Aspect 2. The composition defined in aspect 1, wherein the transitionmetal compound or the transition metal compound of the phosphinetransition metal compound complex comprises a rhodium compound.

Aspect 3. The composition defined in aspect 1, wherein the transitionmetal compound or the transition metal compound of the phosphinetransition metal compound complex comprises an olefin rhodium alkoxidecomplex.

Aspect 4. The composition defined in aspect 1, wherein the transitionmetal compound or the transition metal compound of the phosphinetransition metal compound complex comprises a cyclodiene rhodiumalkoxide complex.

Aspect 5. The composition defined in any one of aspects 1-4, wherein thephosphine or the phosphine of the phosphine transition metal compoundcomplex comprises any suitable alkyl phosphine and/or aryl phosphine.

Aspect 6. The composition defined in any one of aspects 1-4, wherein thephosphine or the phosphine of the phosphine transition metal compoundcomplex is a diphosphine having structure (I):

wherein:

L¹ is a linking group; and

each R independently is H or a C₁ to C₁₈ hydrocarbyl group, a C₁ to C₁₈hydrocarboxy group, or a C₁ to C₁₈ hydrocarbylaminyl group.

Aspect 7. The composition defined in any one of aspects 1-4, wherein thephosphine or the phosphine of the phosphine transition metal compoundcomplex is a diphosphine comprising a 1,6-bisphosphinylhexane, asubstituted 1,6-bisphosphinylhexane, a(1,3-phenylenedi-1,1-ethanediyl)bis(phosphine), a substituted(1,3-phenylenedi-1,1-ethanediylbis(phosphine), a1,8-anthracenediylbis(phosphine), a substituted1,8-anthracenediylbis(phosphine), a1,8-tetradecahydroanthracenediylbis(phosphine), or a substituted1,8-tetradecahydroanthracenediylbis(phosphine), a(methylenedi-2,1-phenylene)bis(phosphine), a substituted(methylenedi-2,1-phenylene)bis(phosphine), a9H-xanthene-4,5-diylbis(phosphine), a substituted9H-xanthene-4,5-diylbis(phosphine), or a combination thereof.

Aspect 8. The composition defined in any one of aspects 1-4, wherein thephosphine or the phosphine of the phosphine transition metal compoundcomplex is a diphosphine having any one of the following structures:

wherein:

Ph is a phenyl group;

Me is a methyl group;

Ar is an aromatic group;

each R independently is H or a C₁ to C₁₈ hydrocarbyl group, a C₁ to C₁₈hydrocarboxy group, or a C₁ to C₁₈ hydrocarbylaminyl group; and

L is a linking group.

Aspect 9. The composition defined in any one of aspects 1-8, wherein theheteroatomic acid or heteroatomic acid derivative comprises a carboxylicacid, an alcohol, a mineral acid, an ammonium salt, an amine, a thiol,etc., or any combination thereof.

Aspect 10. The composition defined in any one of aspects 1-8, whereinthe heteroatomic acid or heteroatomic acid derivative comprises benzoicacid or a substituted benzoic acid, or a salt or ester of benzoic acidor a substituted benzoic acid.

Aspect 11. The composition defined in any one of the preceding aspects,wherein the molar ratio of the transition metal of the transition metalcompound to the phosphine (or diphosphine) is in a range from about0.2:1 to about 5:1 (or have any other minimum value, maximum value, orrange described herein).

Aspect 12. The composition defined in any one of the preceding aspects,wherein the molar ratio of the transition metal of the transition metalcompound or the phosphine transition metal compound complex to theheteroatomic acid or heteroatomic acid derivative is in a range fromabout 0.8:1 to about 5:1 (or have any other minimum value, maximumvalue, or range described herein).

Aspect 13. The composition defined in any one of the preceding aspects,wherein the catalyst composition further comprises an acceptor.

Aspect 14. The composition defined in aspect 13, wherein the acceptor(e.g., acceptor olefin) comprises a mono-olefin compound (e.g.,ethylene, norbornene), a di-olefin compound (e.g., cyclooctadiene,norbornadiene), a tri-olefin compound (e.g., cyclododecatriene), or anycombination thereof.

Aspect 15. The composition defined in aspect 13 or 14, wherein theacceptor (e.g., acceptor olefin) is an aliphatic hydrocarbon compound.

Aspect 16. The composition defined in aspect 13 or 14, wherein theacceptor (e.g., acceptor olefin) is a heteroatomic olefin compound,e.g., an enone, an enamine, an enol, an enamide (acrylamide), etc., orany combination thereof.

Aspect 17. The composition defined in any one of aspects 13-16, whereinthe acceptor (e.g., acceptor olefin) is a cyclic compound.

Aspect 18. The composition defined in aspect 13, wherein the acceptorcomprises an unsaturated triglyceride or an unsaturated natural sourceoil, e.g., soybean oil, corn oil, castor bean oil, canola oil, or anycombination thereof.

Aspect 19. The composition defined in aspect 13, wherein the acceptorcomprises an aliphatic mono-olefin hydrocarbon, an aliphatic di-olefinhydrocarbon, an aliphatic tri-olefin hydrocarbon, or any combinationthereof.

Aspect 20. A dehydroxymethylation process comprising: contacting asaturated linear C₃-C₃₆ hydrocarbon primary alcohol with the catalystcomposition defined in any one of aspects 1-19 to form a C₂-C₃₅ normalalpha olefin.

Aspect 21. A dehydroxymethylation process comprising: contacting asaturated linear C₄-C₃₆ hydrocarbon terminal vicinal diol with thecatalyst composition defined in any one of aspects 1-19 to form a C₂-C₃₄normal alpha olefin.

Aspect 22. A dehydroformylation process comprising: contacting asaturated linear C₃-C₃₆ hydrocarbon aldehyde with the catalystcomposition defined in any one of aspects 1-19 to form a C₂-C₃₅ normalalpha olefin.

Aspect 23. The process defined in any one of aspects 20-22, wherein thestep of contacting is performed in a solvent (e.g., toluene, THF,dioxane).

Aspect 24. The process defined in any one of aspects 20-23, wherein thestep of contacting is performed at a temperature from about 0° C. toabout 150° C. (or any other minimum temperature, maximum temperature, ortemperature range described herein).

Aspect 25. The process defined in any one of aspects 20-24, wherein amolar ratio of the acceptor to the primary alcohol (or vicinal diol, orlinear aldehyde) is in a range from about 0.2:1 to about 1000:1, or fromabout 0.5:1 to about 5:1 (or have any other minimum value, maximumvalue, or range described herein).

Aspect 26. The process defined in any one of aspects 20-25, wherein amolar ratio of the primary alcohol (or vicinal diol, or linear aldehyde)to the transition metal of the transition metal compound or thephosphine transition metal compound complex is in a range from about 2:1to about 1000:1, or from about 10:1 to about 250:1 (or have any otherminimum value, maximum value, or range described herein).

Aspect 27. The process defined in any one of aspects 20-26, wherein amolar yield of the normal alpha olefin is at least about 20%, at leastabout 50%, at least about 75%, or at least about 90%, based on theprimary alcohol (or vicinal diol, or linear aldehyde) (or have any othervalue, or range described herein).

Aspect 28. The process defined in any one of aspects 20-27, wherein thenormal alpha olefin comprises a C₄-C₁₆ normal alpha olefin.

Aspect 29. The process defined in any one of aspects 20-27, wherein thenormal alpha olefin comprises ethylene, propylene, 1-butene, 1-pentene,1-hexene, 1-heptene, 1-octene, 1-nonene, 1-decene, 1-dodecene,1-tetradecene, 1-hexadecene, 1-octadecene, or any combination thereof.

Aspect 30. The process defined in any one of aspects 20-27, wherein thenormal alpha olefin comprises 1-butene, 1-hexene, 1-octene, 1-decene,1-dodecene, or any combination thereof.

Aspect 31. A process comprising:

(i) conducting a hydroboration-oxidation reaction of a first normalalpha olefin having the structure CH₃(CH₂)_(n)HC═CH₂ to form a linearprimary alcohol having the structure CH₃(CH₂)_(n+1)CH₂OH; and

(ii) contacting the linear primary alcohol with the catalyst compositiondefined in any one of aspects 1-19 to form a second normal alpha olefinhaving the structure CH₃(CH₂)_(n−1)HC═CH₂;

wherein n is an integer from 1 to 33.

Aspect 32. A process comprising:

(i) conducting a dihydroxylation reaction of a first normal alpha olefinhaving the structure CH₃(CH₂)_(n)HC═CH₂ to form a terminal vicinal diolhaving the structure CH₃(CH₂)_(n)CH(OH)CH₂OH; and

(ii) contacting the terminal vicinal diol with the catalyst compositiondefined in any one of aspects 1-19 to form a second normal alpha olefinhaving the structure CH₃(CH₂)_(n−2)HC═CH₂;

wherein n is an integer from 2 to 33.

Aspect 33. The process defined in aspect 31 or 32, wherein step (ii) isperformed in a solvent (e.g., toluene, THF, dioxane).

Aspect 34. The process defined in any one of aspects 31-33, wherein step(ii) is performed at a temperature from about 0° C. to about 150° C. (orany other minimum temperature, maximum temperature, or temperature rangedescribed herein).

Aspect 35. The process defined in any one of aspects 31-34, wherein amolar ratio of the acceptor to the primary alcohol (or vicinal diol) isin a range from about 0.2:1 to about 1000:1, or from about 0.5:1 toabout 5:1 (or have any other minimum value, maximum value, or rangedescribed herein).

Aspect 36. The process defined in any one of aspects 31-35, wherein amolar ratio of the primary alcohol (or vicinal diol) to the transitionmetal of the transition metal compound or the phosphine transition metalcompound complex is in a range from about 2:1 to about 1000:1, or fromabout 10:1 to about 250:1 (or have any other minimum value, maximumvalue, or range described herein).

Aspect 37. The process defined in any one of aspects 31-36, wherein amolar yield of the normal alpha olefin is at least about 20%, at leastabout 50%, at least about 75%, or at least about 90%, based on theprimary alcohol (or vicinal diol) (or have any other value, or rangedescribed herein).

Aspect 38. The process defined in any one of aspects 31-37, wherein n isan integer from 2 to 10.

Aspect 39. The process defined in any one of aspects 31-37, wherein n isan integer from 3 to 7.

Aspect 40. The process defined in any one of aspects 31-37, wherein thesecond normal alpha olefin comprises propylene, 1-butene, 1-pentene,1-hexene, 1-heptene, 1-octene, 1-nonene, 1-decene, 1-dodecene,1-tetradecene, 1-hexadecene, 1-octadecene, or any combination thereof.

Aspect 41. The process defined in any one of aspects 31-37, wherein thesecond normal alpha olefin comprises 1-butene, 1-hexene, 1-octene,1-decene, 1-dodecene, or any combination thereof.

Aspect 42. A process comprising:

(i) contacting a first normal alpha olefin having the structureCH₃(CH₂)_(n)HC═CH₂ and a metathesis catalyst system to form a linearinternal olefin having the structure CH₃(CH₂)_(n)HC═CH(CH₂)_(n)CH₃;

(ii) contacting the linear internal olefin with a hydroformylationcatalyst system, carbon monoxide, and hydrogen to form a linear aldehydehaving the formula CH₃(CH₂)_(2n+3)C(═O)H; and

(iii) contacting the linear aldehyde with the catalyst compositiondefined in any one of aspects 1-19 to form a second normal alpha olefinhaving the structure CH₃(CH₂)_(2n+1)HC═CH₂;

wherein n is an integer from 0 to 15.

Aspect 43. A process comprising:

(a) contacting a linear internal olefin having the structureCH₃(CH₂)_(p)HC═CH(CH₂)_(q)CH₃ with a hydroformylation catalyst system,carbon monoxide, and hydrogen to form a linear aldehyde having theformula CH₃(CH₂)_(p+q+3)C(═O)H; and

(b) contacting the linear aldehyde with the catalyst composition definedin any one of aspects 1-19 to form a normal alpha olefin having thestructure CH₃(CH₂)_(p+q+1)HC═CH₂;

wherein p and q independently are an integer from 0 to 15.

Aspect 44. The process defined in aspect 42 or 43, wherein step (iii)and step (b) are performed in a solvent (e.g., toluene, THF, dioxane).

Aspect 45. The process defined in any one of aspects 42-44, wherein step(iii) and step (b) are performed at a temperature from about 0° C. toabout 150° C. (or any other minimum temperature, maximum temperature, ortemperature range described herein).

Aspect 46. The process defined in any one of aspects 42-45, wherein amolar ratio of the acceptor to the linear aldehyde is in a range fromabout 0.2:1 to about 1000:1, or from about 0.5:1 to about 5:1 (or haveany other minimum value, maximum value, or range described herein).

Aspect 47. The process defined in any one of aspects 42-46, wherein amolar ratio of the linear aldehyde to the transition metal of thetransition metal compound or the phosphine transition metal compoundcomplex is in a range from about 2:1 to about 1000:1, or from about 10:1to about 250:1 (or have any other minimum value, maximum value, or rangedescribed herein).

Aspect 48. The process defined in any one of aspects 42-47, wherein amolar yield of the normal alpha olefin is at least about 20%, at leastabout 50%, at least about 75%, or at least about 90%, based on thelinear aldehyde (or have any other value, or range described herein).

Aspect 49. The process defined in any one of aspects 42-48, wherein n,p, and q independently are an integer from 0 to 10.

Aspect 50. The process defined in any one of aspects 42-48, wherein n,p, and q independently are an integer from 1 to 7.

Aspect 51. The process defined in any one of aspects 42-48, wherein thenormal (or second normal) alpha olefin comprises ethylene, propylene,1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, 1-nonene, 1-decene,1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene, or anycombination thereof.

Aspect 52. The process defined in any one of aspects 42-48, wherein thenormal (or second normal) alpha olefin comprises 1-butene, 1-hexene,1-octene, 1-decene, 1-dodecene, or any combination thereof.

What is claimed is:
 1. A process comprising: (i) conducting adihydroxylation reaction of a first normal alpha olefin having thestructure CH₃(CH₂)_(n)HC═CH₂ to form a terminal vicinal diol having thestructure CH₃(CH₂)_(n)CH(OH)CH₂OH; and (ii) contacting the terminalvicinal diol with a catalyst composition to form a second normal alphaolefin having the structure CH₃(CH₂)_(n−2)HC═CH₂; wherein n is aninteger from 2 to 33; and wherein the catalyst composition comprises:(I) a transition metal compound, a phosphine, and a heteroatomic acid orheteroatomic acid derivative; or (II) a phosphine transition metalcompound complex and a heteroatomic acid or heteroatomic acidderivative.
 2. The process of claim 1, wherein: the second normal alphaolefin comprises 1-hexene, 1-octene, 1-decene, 1-dodecene,1-tetradecene, 1-hexadecene, 1-octadecene, or any combination thereof;the transition metal compound or the transition metal compound of thephosphine transition metal compound complex comprises an olefin rhodiumalkoxide complex; and the heteroatomic acid or heteroatomic acidderivative comprises a carboxylic acid, an alcohol, a mineral acid, anammonium salt, an amine, a thiol, or any combination thereof.
 3. Theprocess of claim 2, wherein: a molar ratio of the vicinal diol to thetransition metal of the transition metal compound or the phosphinetransition metal compound complex is in a range from about 2:1 to about1000:1; and the heteroatomic acid or heteroatomic acid derivativecomprises benzoic acid or a substituted benzoic acid, or a salt or esterof benzoic acid or a substituted benzoic acid.
 4. The process of claim1, wherein the catalyst composition further comprises an acceptor. 5.The process of claim 3, wherein the acceptor comprises an enone, anenamine, an enol, an enamide, or any combinations thereof.
 6. Theprocess of claim 3, wherein: the second normal alpha olefin comprises1-hexene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene,1-octadecene, or any combination thereof; and a molar ratio of theacceptor to the vicinal diol is in a range from about 0.2:1 to about1000:1.
 7. The process of claim 6, wherein a molar yield of the secondnormal alpha olefin is at least about 50%, based on the vicinal diol. 8.The process of claim 6, wherein: the transition metal compound or thetransition metal compound of the phosphine transition metal compoundcomplex comprises an olefin rhodium alkoxide complex; and theheteroatomic acid or heteroatomic acid derivative comprises a carboxylicacid, an alcohol, a mineral acid, an ammonium salt, an amine, a thiol,or any combination thereof.
 9. The process of claim 8, wherein: theheteroatomic acid or heteroatomic acid derivative comprises benzoic acidor a substituted benzoic acid, or a salt or ester of benzoic acid or asubstituted benzoic acid.
 10. A process comprising: (i) contacting afirst normal alpha olefin having the structure CH₃(CH₂)_(n)HC═CH₂ and ametathesis catalyst system to form a linear internal olefin having thestructure CH₃(CH₂)_(n)HC═CH(CH₂)_(n)CH₃; (ii) contacting the linearinternal olefin with a hydroformylation catalyst system, carbonmonoxide, and hydrogen to form a linear aldehyde having the formulaCH₃(CH₂)_(2n+3)C(═O)H; and (iii) contacting the linear aldehyde with acatalyst composition to form a second normal alpha olefin having thestructure CH₃(CH₂)_(2n+1)HC═CH₂; wherein n is an integer from 0 to 15;and wherein the catalyst composition comprises: (I) a transition metalcompound, a phosphine, a heteroatomic acid or heteroatomic acidderivative, and an acceptor; or (II) a phosphine transition metalcompound complex, a heteroatomic acid or heteroatomic acid derivative,and an acceptor.
 11. The process of claim 10, wherein: the second normalalpha olefin comprises 1-hexene, 1-octene, 1-decene, 1-dodecene,1-tetradecene, 1-hexadecene, 1-octadecene, or any combination thereof;and a molar ratio of the acceptor to the linear aldehyde is in a rangefrom about 0.2:1 to about 1000:1.
 12. The process of claim 11, whereinthe acceptor comprises an enone, an enamine, an enol, an enamide, or anycombinations thereof.
 13. The process of claim 11, wherein: a molaryield of the second normal alpha olefin is at least about 50%, based onthe linear aldehyde; the transition metal compound or the transitionmetal compound of the phosphine transition metal compound complexcomprises an olefin rhodium alkoxide complex; and the heteroatomic acidor heteroatomic acid derivative comprises a carboxylic acid, an alcohol,a mineral acid, an ammonium salt, an amine, a thiol, or any combinationthereof.
 14. The process of claim 11, wherein: the heteroatomic acid orheteroatomic acid derivative comprises benzoic acid or a substitutedbenzoic acid, or a salt or ester of benzoic acid or a substitutedbenzoic acid.
 15. A process comprising: (a) contacting a linear internalolefin having the structure CH₃(CH₂)_(p)HC═CH(CH₂)_(q)CH₃ with ahydroformylation catalyst system, carbon monoxide, and hydrogen to forma linear aldehyde having the formula CH₃(CH₂)_(p+q+3)C(═O)H; and (b)contacting the linear aldehyde with a catalyst composition to form anormal alpha olefin having the structure CH₃ (CH₂)_(p+q+1)HC═CH₂;wherein p and q independently are an integer from 0 to 15; and whereinthe catalyst composition comprises: (I) a transition metal compound, aphosphine, a heteroatomic acid or heteroatomic acid derivative, and anacceptor; or (II) a phosphine transition metal compound complex, aheteroatomic acid or heteroatomic acid derivative, and an acceptor. 16.The process of claim 15, wherein: the second normal alpha olefincomprises 1-hexene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene,1-hexadecene, 1-octadecene, or any combination thereof; and a molarratio of the acceptor to the linear aldehyde is in a range from about0.2:1 to about 1000:1.
 17. The process of claim 16, wherein the acceptorcomprises an enone, an enamine, an enol, an enamide, or any combinationsthereof.
 18. The process of claim 16, wherein: a molar yield of thesecond normal alpha olefin is at least about 50%, based on the linearaldehyde; the transition metal compound or the transition metal compoundof the phosphine transition metal compound complex comprises an olefinrhodium alkoxide complex; and the heteroatomic acid or heteroatomic acidderivative comprises a carboxylic acid, an alcohol, a mineral acid, anammonium salt, an amine, a thiol, or any combination thereof.
 19. Theprocess of claim 16, wherein: the heteroatomic acid or heteroatomic acidderivative comprises benzoic acid or a substituted benzoic acid, or asalt or ester of benzoic acid or a substituted benzoic acid.